Polyamide nanoparticles and uses thereof

ABSTRACT

Nanoparticles of N-halamine-derivatized crosslinked polyamide. Process of preparing the polymeric nanoparticles per se and incorporated in or on a substrate. Uses of the polymeric nanoparticles and of substrates incorporating same, particularly for reducing a formation of organic-based contaminants, e.g., load of a microorganism or of a biofilm.

FIELD OF THE INVENTION

The present invention, in some embodiments thereof, relates to nanosizedcrosslinked polymeric backbones, and more particularly, but notexclusively, to nanosized N-halamine-derivatized crosslinked polyamideand uses thereof in, for example, reducing or preventing organic-basedcontaminant.

BACKGROUND OF THE INVENTION

Various organic antimicrobial agents, such as quaternary ammonium salts,phosphonium salts, and N-halamine compounds, have been extensivelyinvestigated over the past 20 years. Compared with halogens, which areinorganic, N-halamines are more stable and less corrosive, and theirnumerous sought-after qualities (i.e., effectiveness at killing toward abroad spectrum of microorganisms, long-term stability, the possibilityof recycling, low cost, and safety for humans and the environment) makeN-halamines particularly attractive. The dissociation constant ofN-halamine compounds in water is relatively low and varies based onchemical structure in the order amine<amide<imide. However, in thepresence of microorganisms, oxidative halogen e.g., Cl transfer from theN-halamine bond to the microorganism is significantly favored overhydrolysis. Amine-halamine is the most stable of all halamine bonds buthas a slower bactericidal rate than amide-halamine. In contrast,imide-halamine has a rapid bactericidal rate because it is the leaststable of all halamine bonds and can rapidly release active Cl into themedium.

Compounds containing amide-halamine bonds are considered the mostpractical for industrial applications because they exhibit a moderaterate of transfer of the oxidative Cl from the N-halamine to bacteria inaqueous solution and thus provide reasonably rapid bactericidalactivity. Although the hydrolysis constant of amidehal amines is in therange of 10⁻⁸, the Cl transfer to the bacteria is the more favorableprocess.

Bacterial attachment to surfaces leading to the formation of communitiesof bacterial cells is a major problem in many diverse settings. Thissessile community of microorganisms, also termed a biofilm, is attachedto an interface, or to each other, and embedded in an exopolymericmatrix. It manifests an altered mode of growth and transcribes genesthat free-living microorganisms do not transcribe. The mostcharacteristic phenotype of the biofilm mode of growth is its inherentresistance to disinfection, antimicrobial treatment and immune responsekilling.

The inherent resistance of biofilms to killing and their pervasiveinvolvement in product contamination, pipe clogging and implant-relatedinfections has prompted for various industrial applications such asdrinking water distribution systems and food packaging.

U.S. Pat. No. 8,211,361 discloses one or more acyclic-amine structuresbeing halogenated to form one or more acyclic N-halamine structure, anduses same for functionalizing a surface of an object to controlmicrobial contamination of a surface.

CN Patent No. 103,044,611 discloses polymeric antibacterialnano-particles and magnetic antibacterial nano-particles containinghalamine functional groups.

SUMMARY OF THE INVENTION

In a search for novel methodologies for fabricating long-lasting organicantimicrobial agents, the present inventors have developed a novelnanosized crosslinked polymers, and more particularly, but notexclusively, N-halamine-derivatized crosslinked polyamide nanoparticles(NPs). The present inventors have further surprisingly uncovered thatfollowing halogenations of the nanosized crosslinked polyamide polymers,such nanoparticles can inhibit both bacterial growth and withstand harshconditions (e.g., high organic loads) while maintaining remarkablestability and durability to organic reagents and to repetitive bacterialloading cycles as compared with the common disinfectant.

The present inventors have further successfully utilized nanosizedN-halamine-derivatized crosslinked polyamide nanoparticles for impartinganti-biofouling properties to various surfaces.

According to an aspect of some embodiments of the present inventionthere is provided a composition-of-matter comprising a plurality ofcrosslinked polymeric backbones, wherein at least 80% of the pluralityof crosslinked polymeric backbones is characterized by an averagehydrodynamic diameter of less than 500 nm, the crosslinked polymericbackbones being represented by the general Formula I:([A₁]_(x)[A₂]_(y))B_(n)wherein:(a) A₁ is a monomeric unit derived from a secondary diamide compound,the secondary diamide compound being represented by the general formulaII:

R₁ and R₃ are hydrogen or a methyl group; andR₂ is C1-C4 alkyl group;(b) A₂ is a monomeric unit being a primary amide selected from the groupconsisting of: acrylamide, alkylacrylamide, and any derivative thereof;(c) each of the plurality of polymeric backbones is crosslinked by atleast one A₁;(d) B, in each instance, is a halogen atom independently selected fromthe group consisting of Cl, Br, and I optionally being bound to thenitrogen belonging to A₁ and/or to A₂;(e) x and y are integers, independently, representing the total numbersof A₁ and A₂, respectively, in the plurality of crosslinked polymericbackbones, the x and/or the y having a value of at least 5; and(f) n represents the total numbers of said B.

According to some embodiments, A2 is methacrylamide. According to someembodiments, A₁ is selected from the group consisting of: N,N-methylenebisacrylamide, N,N-ethylene bisacrylamide, and any derivative thereof.In some embodiments, A₁ is N,N-methylene bisacrylamide.

In some embodiments, B is Cl. In some embodiments, B is Br.

In some embodiments, n has a value such that n/(x+y) multiplied by 100is at least 0.1.

According to some embodiments, the plurality of crosslinked polymericbackbones is characterized by an average hydrodynamic diameter of lessthan 50 nm with a size distribution of that varies within a range ofless than 20%.

According to some embodiments, the plurality of crosslinked polymericbackbones is prepared by co-polymerizing a plurality of the monomericunits A₁ and A₂ in a weight ratio of A₁ to A₂ that ranges from about 1/9to about 6/4 in a surfactant-free dispersion comprising at least onewater soluble initiator, selected from the group consisting of:AIBNCO₂H, PPS, AIBN, and H₂O₂.

According to some embodiments, the plurality of crosslinked polymericbackbones is further subjected to a step of halogenation, thehalogenation being chlorination and/or bromination, and/or iodination.

According to some embodiments, the composition-of-matter is in form ofdry powder. In some embodiments, the composition-of-matter isincorporated within a formulation. In some embodiments, thecomposition-of-matter further comprises a substrate, wherein theplurality of crosslinked polymeric backbones is incorporated or coatedin/on at least a portion of the substrate. In some embodiments, thesubstrate is or forms a part of an article. In some embodiments,substrate comprises or is made of a polymer, wood, a metal, glass,carbon, a biopolymer and/or silicon.

According to an aspect of some embodiments of the present invention,there is provided an article of comprising the composition-of-matter asdescribed herein. In some embodiments, the article is selected from thegroup consisting of a medical device, organic waste processing device,fluidic device, water system device, tubing, an agricultural device, apackage, a sealing article, a fuel container and a construction element.

According to an aspect of some embodiments of the present invention,there is provided method of inhibiting or reducing a formation of loadof organic-based contaminant on or within an article, the methodcomprising incorporating or coating the composition-of-matter asdescribed herein. In some embodiments, the article is selected from thegroup consisting of: a medical device, an organic waste processingdevice, a fluidic device, a water system device, an agricultural device,a package, a sealing article, a fuel container and a constructionelement. In some embodiments, the load of organic-based contaminant ismaintained substantially reduced after at least onedehalogenation-rehalogenation cycle with the halogen atom.

According to some embodiments, the load of organic-based contaminant isa load of a microorganism, and/or a formation of a biofilm or biofoulingin and/or on an article.

In some embodiments, the load of organic-based contaminant is maintainedsubstantially reduced over a period of up to at least six months.

In some embodiments, the microorganism is selected from the groupconsisting of: viruses, fungi, parasites, yeast, bacteria, and protozoa.In some embodiments, the microorganism is a bacterium selected from thegroup consisting of: Gram positive bacteria, and Gram negative bacteria.In some embodiments, the microorganism is a bacterium selected from thegroup consisting of Gram negative bacteria.

According to some embodiments, the method further comprises one or moredehalogenating-rehalogenating cycles with halogen atoms selected fromthe group consisting of Cl, Br, and I.

According to an aspect of some embodiments of the present inventionthere is provided a process of preparing the composition-of-matter asdescribed herein, the process comprising: co-polymerizing a plurality ofthe monomeric units A₁ and A₂, the co-polymerizing comprising dispersingsaid monomeric units in a weight ratio of A₁/A₂ that ranges from about1/9 to about 6/4 in a surfactant-free aqueous phase comprising at one ormore water soluble initiators, to thereby obtain a plurality ofcrosslinked polymeric backbones characterized by an average hydrodynamicdiameter of less than 500 nm with a size distribution of that varieswithin a range of less than 20%.

In some embodiments, the one or more initiators are selected from thegroup consisting of: AIBNCO₂H, H₂O₂ PPS and AIBN. In some embodiments,the surfactant-free aqueous phase further comprising one or morereducing agent selected from the group consisting of: a sulfite, abisulfite, thiosulfate, formamidinesulfinic acid, and ascorbic acid.

According to some embodiments, the surfactant-free aqueous phase issubjected to temperature that ranges from about 20° C. to about 100° C.

According to some embodiments, the process further comprises a step ofat least partially halogenating the polymeric material. In someembodiments, the step of halogenating comprises the addition of a halidesource. In some embodiments, the halide source is a salt of a materialselected from the group consisting of: di-X-isocyanurate, hypo-halite,N—X-succinimide, or hypo-halite, wherein the halite and X each isselected from the group consisting of: Cl, I or Br. In some embodiments,the halide source is hypochlorite. In some embodiments, the halidesource is dichlorocyanuric acid (DCCA).

Unless otherwise defined, all technical and/or scientific terms usedherein have the same meaning as commonly understood by one of ordinaryskill in the art to which the invention pertains. Although methods andmaterials similar or equivalent to those described herein can be used inthe practice or testing of embodiments of the invention, exemplarymethods and/or materials are described below. In case of conflict, thepatent specification, including definitions, will control. In addition,the materials, methods, and examples are illustrative only and are notintended to be necessarily limiting.

BRIEF DESCRIPTION OF THE DRAWINGS

Some embodiments of the invention are herein described, by way ofexample only, with reference to the accompanying drawings. With specificreference now to the drawings in detail, it is stressed that theparticulars shown are by way of example and for purposes of illustrativediscussion of embodiments of the invention. In this regard, thedescription taken with the drawings makes apparent to those skilled inthe art how embodiments of the invention may be practiced.

In the drawings:

FIG. 1 is a schematic illustration of the methacrylamide (MAA) andN,N-methylene bisacrylamide (MBAA) chemical structures and thepolymerization and the chlorination process;

FIGS. 2A-C are graphs of fourier transform infrared (FTIR) spectra ofthe monomer MAA (FIG. 2A) and the P(MAA-MBAA) (FIG. 2B) andP(MAA-MBAA)-Cl (FIG. 2C) polymeric nanoparticles as prepared.

FIG. 3 is a graph showing the thermogravimetric analysis (TGA) ofP(MAA-MBAA) nanoparticles before (solid line) and after (dotted line)chlorination of (MAA-MBAA)-Cl nanoparticles.

FIGS. 4A-B present cryogenic transmission electron microscopy (cryo-TEM)image (FIG. 4A; bar is 100 nm) and hydrodynamic size histogram (FIG. 4B)of the P(MAA-MBAA) nanoparticles.

FIG. 5 presents a graph showing the influence of the total monomer[MAA+MBAA] concentration on the diameter of the P(MAA-MBAA)nanoparticles. The P(MAA-MBAA) nanoparticles were prepared in thepresence of different total monomer concentrations.

FIGS. 6A-B present point graphs showing the influence of the type andconcentration of potassium persulfate (PPS) (FIG. 6A), andazobisisobutylonitrile (AIBN) (FIG. 6B) initiators, on the diameter ofthe P(MAA-MBAA) nanoparticles. The P(MAA-MBAA) nanoparticles wereprepared in the presence of different concentrations of PPS or AIBN, asindicated herein below.

FIG. 7 presents a point graph showing the influence of the weight ratio[MBAA]/[MAA] on the size and size distribution of P(MAA-MBAA)nanoparticles prepared by holding the total monomer concentrationsconstant (2%) while varying the weight ratio [MBAA]/[MAA].

FIGS. 8A-B are point graphs showing the influence of the polymerizationtemperature on the diameter (FIG. 8A) and the yield of formation (FIG.8B) of P(MAA-MBAA) nanoparticles prepared at different temperatures. Theyield curve was constructed in triplicate with approximately 10%standard deviation (SD).

FIGS. 9A-B are point graphs demonstrating the kinetics (FIG. 9A) andyield (FIG. 9B) of the formation of the P(MAA-MBAAA) nanoparticlesprepared as described below. The yield curve displays data collected intriplicate with approximately 10% SD.

FIG. 10 presents a point graph showing the influence of the NaOClconcentration on the Cl loading content of the P(MAA-MBAA)-Clnanoparticles as prepared.

FIG. 11 presents a point graph showing the influence of the chlorinationtime on the Cl content of the P(MAA-MBAA)-Cl nanoparticles as preparedand further chlorinated.

FIG. 12 presents a point graph showing the influence of the chlorinationtemperature on the Cl content of the P(MAA-MBAA) nanoparticles asprepared and thereafter chlorinated.

FIG. 13 presents a point graph showing the % bound Cl content of theP(MAA-MBAA)-Cl nanoparticles stored for different periods of time underlaboratory light conditions before (black dots) and after (open circledots) rechlorination.

FIG. 14 presents a point graph showing the % bound Cl content of theP(MAA-MBAA)-Cl nanoparticles irradiated with UVA light for differentperiods of time before (black dots) and after (open circle dots)rechlorination.

FIGS. 15A-D present graphs showing x-ray diffraction (XRD) patterns ofthe monomers MAA (FIG. 15A), MBAA (FIG. 15B) and the polymerized NPsP(MAA-MBAA) (FIG. 15C) and the charged ones with Cl (FIG. 15D).

FIG. 16 presents cryo-transmission electron microscopy (TEM) image ofthe P(MAA-MBAA)-Cl NPs, with arrows marking the NPs, as preparedaccording to some embodiments of the present invention. Bar is 100 nm.

FIGS. 17A-B present bar graphs presenting the activity of P(MAA-MBAA)-ClNPs and NaPCl following repetitive bacterial loading cycles for E. coli(FIG. 17A) and for S. aureus (FIG. 17B) treated with eitherP(MAA-MBAA)-Cl NPs, NaOCl, or being untreated. Every hour aliquots wereremoved from each sample and plated on agar plates. In parallel, 10⁵CFU/ml (CFU: Colony-forming unit) freshly prepared bacteria were added.After the eighth loading cycle, the tubes were left in the shaker andsamples taken the following day. Error bars represent the standarddeviation of three independent experiments. It is to note that since theP(MAA-MBAA)-Cl were able to kill all the bacteria at all the indicatedtime points, the grey bars are not shown in the graphs.

FIGS. 18A-B present graphs showing kinetic curves of E. coli (FIG. 18A)and S. aureus (FIG. 18B) killing in the presence of increasingconcentrations of the P(MAA-MBAA)-Cl nanoparticles. The growth curves ofuntreated bacteria or bacteria incubated with 1% P(MAA-MBAA)nanoparticles are also shown. These results represent the trend observedin at least three independent experiments.

FIG. 19 presents a bar graph showing the antibacterial activity ofP(MAA-MBAA)-Cl nanoparticles (0.6% w/v, 0.1 M Cl concentration) preparedas described in the experimental section against multiple drugresistance (MDR) bacterial strains of Providencia stuartii, Klebsiellapneumonia, and E. coli. The bacterial strains were grown overnight andtreated as described in the Examples section.

FIGS. 20A-B present graphs showing killing kinetic curves, as obtainedfrom experiments being conducted at least three independent times, of E.coli (FIG. 20A) and S. aureus (FIG. 20B) in the presence of eitherP(MAA-MBAA)-Cl or NaOCl. The growth curves of untreated bacteria orbacteria incubated with P(MAA-MBAA) NPs are displayed as well.

FIG. 21 presents a bar graph showing oxidative stress induced byP(MAA-MBAA)-Cl NPs. E. coli strains bearing a promoter-lux fusion foroxidative stress related genes, i.e., micF or sodA, were exposed to 5.5mM oxidative chlorine found on the P(MAA-MBAA)-Cl NPs for 8 h. Bacteriatreated with either sterile water or P(MAA-MBAA) NPs served as negativecontrols. Gene expression was monitored by measuring luminescence. Theresults are presented as relative luminescence unites (RLU) as afunction of growth (OD595). Error bars correspond to the standarddeviations of three independent experiments.

FIGS. 22A-B presents transmission electron microscopy (TEM) images of S.aureus bacteria. S. aureus were treated with either P(MAA-MBAA) NPs(left panels) or their chlorinated counterparts (right panels) for 1.5 h(FIG. 22A), and TEM micrographs of S. aureus treated with theP(MAA-MBAA)-Cl NPs for 15′ (FIG. 22B). Bar is 500 nm.

FIGS. 23A-C present hydrodynamic size histogram (FIG. 23A) and thecorresponding cryo-TEM images of the P(MAA-MBAA)-Cl NPs synthesized attwo different sizes i.e., small (left panels) and large (right panels)(FIG. 23B; bar is 200 nm), and TEM micrographs of S. aureus bacteriatreated for 1.5 h with the chlorinated NPs of the two different sizes(FIG. 23C).

FIG. 24 presents scanning electron microscopy (SEM) of S. aureusbacteria treated with P(MAA-MBAA)-Cl NPs for 1.5 h (right panel)vis-a-vis untreated S. aureus bacteria (left panel).

FIG. 25 presents TEM micrographs of E. coli bacteria treated with eitherP(MAA-MBAA) NPs (left panel) or their chlorinated counterparts for 45′(right panel). Bar is 500 nm.

FIG. 26 presents transmission electron microscopy (TEM) images of S.aureus bacteria treated with P(MAA-MBAA)-Cl NPs for 15′. The upper twopanels show S. aureus that were incubated with the chlorinated NPs for15′ at 37° C. (left panel) or at 4° C. (right panel) (followingpre-incubation of the cells for 2 hours at 4° C.). The lower panels showS. aureus that were either boiled for 10′ at 95° C. (left panel) orincubated with DMSO for 1 h before adding the NPs for 15′ (right panel).Bar is 500 nm.

FIG. 27 presents TEM micrographs of S. aureus suspended in LB (leftpanel) or DDW (right panel) followed by the addition of P(MAA-MBAA)-ClNPs for 15′. Bar is 500 nm.

FIG. 28 presents transmission electron microscopy of Saos-2 cellstreated with either P(MAA-MBAA) NPs (upper panel) or their chlorinatedcounterparts (lower panel) for 15′. The pictures show that there is nospecific accumulation of NPs on the cell surface. In the left panels baris 2 μm; in the right panels the bar is 500 nm.

FIG. 29 presents TEM images showing P(MAA-MBAA)-Cl NPs triggeringmorphological changes within the bacteria. S. aureus were treated witheither P(MAA-MBAA) NPs (left panel) or chlorinated counterparts (rightpanel) for 5 h (upper panel) or 15 h (lower panel). The arrows designatemembrane constructs. Bar is 200 nm.

FIGS. 30A-F present graphs demonstrating the short-term stability ofP(MAA-MBAA)-Cl NPs versus NaOCl to organic material. E. coli (FIGS. 30A,30C, 30E) or S. aureus (FIGS. 30B, 30D, 30F) were added to LB media thathad been pre-incubated with either P(MAA-MBAA)-Cl NPs, NaOCl, or leftuntreated for 3 h (FIGS. 30A-B), 5 h (FIGS. 30C-D) or 24 h (FIGS.30E-F). Aliquots were removed after a further 3 h or 24 h incubation andplated on agar plates to determine bacterial viability. Error barsindicate the standard deviation of three independent experiments.

FIGS. 31A-B present bar graphs showing P(MAA-MBAA)-Cl NPs exhibitinglong-term activity and stability to organic materials. E. coli (FIG.31A) or S. aureus (FIG. 31B) were treated with either P(MAA-MBAA)-ClNPs, NaOCl, or were untreated. Each of these reagents was pre-incubatedwith LB medium for 24 h (day 1) following which 10∧5 CFU/ml of therelevant bacteria were added for 24 h (day 2). Every day aliquots wereremoved from each sample and plated on agar plates. In parallel, 10∧5CFU/ml fresh bacteria were added as appropriate. Error bars representthe standard deviation of three independent experiments.

FIG. 32 is a bar graph showing the susceptibility of NaOCl to organicmaterials. Fresh NaOCl solution, taken from a commercial container (0.72M), was incubated with an equivalent volume of LB (reaching a finalconcentration of 0.36 M) for 1 week before addition of either E. coli orS. aureus. Lower concentrations of NaOCl subjected to the same procedureare also presented.

FIGS. 33A-B are bar graphs demonstrating the kinetics of oxidativechlorine release from P(MAA-MBAA)-Cl NPs and NaOCl. Chlorinated NPs andNaOCl were incubated with LB medium and at the stated time points,samples were taken for oxidative chlorine quenching via NaI. Theoxidative chlorine concentrations were determined by spectrophotometermeasurements at 292 nm (FIG. 33A) and 350 nm (FIG. 33B). 0* refers tothe initial oxidative chlorine concentration found on either the NPs orNaOCl in water, i.e., prior to addition of the organic medium.

FIG. 34 is a bar graph showing that P(MAA-MBAA)-Cl NPs do not need toenter the bacteria to exert their killing effect. The chlorinated NPs orDDW (i.e. control) were incubated with LB medium for 10 minutes followedby centrifugation in ultrafiltration tubes (M.W cutoff 30000) that donot allow the NPs to pass through the pores, as determined by DLS. Thefiltrate was then supplemented with either E. coli or S. aureus.

FIG. 35 presents graphs showing electron spin resonance (ESR) spectrademonstrating that P(MAA-MBAA)-Cl NPs provoke formation of hydroxylradicals. ESR spectrum of the DMPO-OH adducts formed upon mixingP(MAA-MBAA)-Cl NPs with LB medium (black line) or distilled water (greyline). The blue line represents P(MAA-MBAA) NPs mixed with LB media.

FIGS. 36A-B are graphs demonstrating that P(MAA-MBAA)-Cl NPs triggerformation of hydroxyl radicals in the presence of organic materials.(FIG. 36A) ESR spectrum of the DMPO-OH adducts formed upon mixingP(MAA-MBAA)-Cl NPs with either LB medium (black line) or Tryptone oryeast extract or NaCl. Quantification of ROS formed in response tomixing LB media or its various components with the chlorinated NPs(calculated from double integration of the DMPO-OH spin adducts quartet)(FIG. 36B).

FIG. 37 is a graph demonstrating the killing effect of P(MAA-MBAA)-ClNPs toward bacteria (E. coli and S. aureus) suspended in water. E. colior S. aureus were incubated overnight with either DDW (i.e. control) orthe chlorinated NPs following which samples were taken and plated onagar plates for determining the bacterial viability.

FIGS. 38A-C present graphs demonstrating that antibacterial activity ofP(MAA-MBAA)-Cl NPs is proportional to the quantity of the radicalsformed. CFU/ml of E. coli and S. aureus exposed to 1.25-10 mM ofP(MAA-MBAA)-Cl NPs or to distilled water (negative control) for 24 h at37° C. (FIG. 38A). ESR spectrum of the DMPO adducts formed upon mixingLB medium with increasing concentrations of oxidative chlorine bound toP(MAA-MBAA)-Cl NPs (1.25-10 mM) (FIG. 38B). Quantification of ROS formedin response to increasing concentrations of the chlorinated NPs(calculated from double integration of the DMPO-OH spin adducts quartet)(FIG. 38C).

FIGS. 39A-C present graphs demonstrating ROS formation upon mixingP(MAA-MBAA)-Cl NPs with LB without (i.e. control) or with addition ofeither 10% DMSO, 10 mM NAC, or 10 mM AA (FIG. 39A). Killing kineticcurves of E. coli (FIG. 39B) and S. aureus (FIG. 39C) in the presence ofP(MAA-MBAA)-Cl NPs that was pre-incubated with either double distilledwater (DDW) (i.e. control) or the indicated antioxidants for 1 h beforeadding the relevant bacteria.

FIG. 40 presents graph demonstrating the kinetic study of methylene blue(MB) degradation by incubation with P(MAA-MBAA)-Cl nanoparticles.

FIG. 41 presents graph demonstrating the kinetic study of crystal violet(CV) degradation by incubation with P(MAA-MBAA)-Cl nanoparticles.

FIG. 42 is a bar graph demonstrating the antibacterial activity ofP(MAA-MBAA)-Cl-coated polyethylene (PET) films. E. coli and S. aureusbacteria were both grown in the presence of P(MAA-MBAA)-Cl-coated PETfilms at increasing coating thicknesses or were left untreated (i.e.control).

FIGS. 43A-E presents incubation of PE/P(MAA-MBAA) profiles in “Shafdan”sewage water. “I” designates chlorination of the profile while “O”designates the non chlorinated profile, in each cycle. Polyethyleneprofiles containing the P(MAA-MBAA) NPs were either chlorinated (left)or not (right) (FIG. 43A). PE/NPs and PE/Cl-NPS profiles in pipes weredipped for the first time for a month in flowed Shafdan waste water(FIG. 43B). A second cycle of chlorination and incubation for anothermonth in Shafdan (FIG. 43C). A third cycle of chlorination andincubation for another month in Shafdan (FIG. 43D). A forth cycle ofchlorination and incubation for two months in Shafdan. the antimicrobialactivity of some embodiments of the composition of the invention in asewage system (FIG. 43E).

FIGS. 44 A-B present bar graphs showing the protein quantification ofthe chlorinated profiles versus the control, with the designation of “I”and “O” as in FIG. 43. FIG. 44A shows the reduction in the proteinlevels of the various profiles through the two cycles and FIG. 44B showsthe proteins levels at the end of the experiment, two months after theforth regeneration cycle was conducted.

FIGS. 45 A-C present drippers containing the P(MAA-MBAA) NPs and theirchlorinated (treated) counterparts following incubation for one month insewage treated irrigation water. FIG. 45A presents photos showing thenon-chlorinated vis-a-vis chlorinated drippers. The total biomass on thedrippers was also imaged using environmnental scanning electronmicroscopy (E-SEM): treated (right, bar is 100 μm and non-treated (left,bar is 500 μm) (FIG. 45B) and quantified via total organic carbon (FIG.45C).

FIG. 46 present photos showing drippers containing the P(MAA-MBAA) NPsthat were left untreated (i.e. control; upper panel) or treated withNaOCl (i.e. treated; middle panel). These drippers were stored inHazerim for 2.5 months, following which the pictures shown were taken.Additionally, drippers that were regenerated with Cl⁺ after one month ofincubation in Hazerim, were put back into the experimental system andincubated for one month in Hazerim (lower panel).

FIGS. 47A-C presents bar graph showing the biocompatibility of profilesimpregnated with P(MAA-MBAA) nanoparticles or uncharged ones. FIG. 47A:BALB/c 3T3 and NR8383 cells were grown in the presence of medium thathad been previously incubated with profiles impregnated with eitherP(MAA-MBAA) or P(MAA-MBAA)-Cl. After 24 h, the cells viability wasdetermined using water soluble Tetrazolium assay (WST-1). FIG. 47B:BALB/c 3T3 cells were used and their viability was examined utilizingneutral red uptake (NRU) assay. FIG. 47C: adenosine triphosphate (ATP)measurements were performed. Control designates cells that were grownwith medium that was not exposed to any profile.

DETAILED DESCRIPTION OF THE INVENTION

The present invention, in some embodiments thereof, relates to nanosizedcrosslinked polymeric backbones, more particularly, but not exclusively,to nanosized N-halamine-derivatized crosslinked polyamide nanoparticles.

Before explaining at least one embodiment of the invention in detail, itis to be understood that the invention is not necessarily limited in itsapplication to the details set forth in the following description orexemplified by the Examples. The invention is capable of otherembodiments or of being practiced or carried out in various ways.

As discussed hereinathroughout, the present inventors have synthesizednanosized cross-linked N-halamine-derivatized polymer followed by achlorination process. A beneficial antimicrobial/antibiofilm activity ofthe polymer was also demonstrated.

The present inventors have also shown that the chlorinated nanosizedcross-linked N-halamine polymer exhibited improved and long-lastingantimicrobial and/or antibiofilm activities, compared to householdbleach solution and compared to non-nanometeric polymer.

According to some embodiments, the polymer of the invention can berepresented by the general formula I:([A₁]_(x)[A₂]_(y))B_(n)

Embodiments of the present invention therefore relate to nanosizedcrosslinked polymeric backbones comprising primary amide (A₂) andsecondary diamide (A1) monomeric units, as described in detailshereinbelow.

As used herein, the term “polymer” describes an organic substancecomposed of a plurality of repeating structural units (monomeric units)covalently connected to one another.

The Compositions-of-Matter:

According to an aspect of some embodiments of the present inventionthere is provided a composition-of-matter comprising a plurality ofuniform nanosized crosslinked polymeric backbones.

By “uniform”, it is meant that at least e.g., 30%, 40%, 50%, 60%, 70%,80%, 90%, 99% of the plurality of the crosslinked polymeric backbones ischaracterized by a nanometric size having less than 15% variation insize.

The crosslinked polymeric backbone is represented by the general FormulaI:([A₁]_(x)[A₂]_(y))B_(n)wherein:

A₁ is a monomeric unit derived from a secondary diamide compound, and A₂is a monomeric unit being a primary amide; x and y are integers,independently, representing the total numbers of A₁ and A₂,respectively; B, in each instance, is a halogen atom independentlyselected from the group consisting of Cl, Br, and I; and n representsthe total numbers of said B. In some embodiments, x is an integerranging from 1 to about 1,000,000, and y is an integer ranging from 1 toabout 1,000,000.

Herein, the term “monomer” refers to a molecule that may bind chemicallyto other molecules to form a polymer.

The terms “monometric unit” refer to the repeat units, derived from thecorresponding monomer. The polymer comprises the monomeric units. By“derived from” it is meant to refer to the compound following thepolymerization process.

The term amide, has a common meaning in the art, and refers to a moietyof structure C(O)NR₁R₂, wherein R₁ and R₂ are independently hydrogen ora substituted or unsubstituted, cyclic or acyclic, linear or branched,saturated or unsaturated aliphatic, heteroaliphatic, aryl or heteroarylmoiety.

The term “secondary diamide” means a carboxamide-containing moleculehaving the two functional groups of —(CO)NHR.

In some embodiments, the secondary amide is derived from a secondarydiamide compound, represented by the general formula II:

such thatR₁ and R₃ are hydrogen or a methyl group; andR₂ is C1-C4 alkyl group.

In some embodiments, R₁ is hydrogen and R₃ is a methyl group. In someembodiments, both R₁ and R₃ are methyl groups. In some embodiments, bothR₁ and R₃ are hydrogens.

In some embodiments, R₂ is a methyl group. In some embodiments, R₂ is anethyl group. In some embodiments, R₂ is a propyl group. In some R₂ is abutyl group.

As used herein, the group of methyl, ethyl, propyl and butyl, may alsorefer to any derivatives thereof. The term “derivative thereof” refersto a compound which retains the basic skeleton. As used herein and inthe art, derivatives are compounds structurally similar to a parentcompound and are derivable from that parent compound while being, insome embodiments, branched-chain of the parent compound. A derivativemay or may not have different chemical or physical properties of theparent compound as long as the activity, e.g., antimicrobial activity isretained. Derivatization (i.e., modification) may involve substitutionof one or more moieties within the molecule (e.g., a change infunctional group) that do not substantially alter the function of themolecule for a desired purpose. The term “derivative” is also used todescribe all solvates, for example hydrates or adducts (e.g., adductswith alcohols), active metabolites, and salts of the parent compound.

In some embodiments, A₂ is a monomer being a primary amide selected fromthe group consisting of: acrylamide, alkylacrylamide, and any derivativethereof. In exemplary embodiments, A₂ is methacrylamide (denoted as“MAA”).

In some embodiments, A₁ is selected from the group consisting of:N,N-methylene bisacrylamide, N,N-ethylene bisacrylamide, any derivativethereof. In exemplary embodiments A₁ is N,N-methylene bisacrylamide(denoted as “MBAA”).

In some embodiments, each of the plurality of polymeric backbones iscrosslinked by at least one A₁.

As used herein, “polymer backbone” refers generally to a polymercomprising monomeric units. It is to be understood that in the contextof the present invention, the term “polymeric backbone” refers to themain chain of polymeric skeleton together with chain branches projectingfrom the polymeric skeleton. The branches may comprise one or more ofeither A₁ and/or A₂ monomeric units as described herein.

The term “crosslinked polymer backbone” or, simply, “crosslinkedpolymer”, refers generally to a polymer which comprises the monomericunits, including the crosslinking bridges.

As used hereinthroughout “P(MAA-MBAA)” denotes the crosslinked polymercomprising the monomeric units of MAA and MBAA. As used herein,“P(MAA-MBAA)-Cl” or “P(MAA-MBAA)-Br” stands for the P(MAA-MBAA)following a chlorination or bromination process, respectively.

As used herein, “crosslinked” and/or “crosslinking”, and any grammaticalderivative thereof refers generally to a chemical process or thecorresponding product thereof in which two chains of polymeric moleculesare attached by bridges (crosslinker) composed of an element, a group ora compound, which join certain carbon atoms of the chains by primarychemical.

Crosslinked polymers have quite different mechanical and physicalproperties than their uncrosslinked linear or branched counterparts. Forexample, crosslinked polymers may show unique and highly desirableproperties such as solvent resistance, high cohesive strength, andelastomeric character. Typically, the crosslinked polymers arecharacterized by a plurality of polymeric strands that may be covalentlylinked together. The term “polymeric strand” refers to any compositionof monomeric units covalently bound to define a backbone.

Typically, but not exclusively, the crosslinking reaction can occur insitu during formation of the polymer.

In the context of the present disclosure the cross linker is a compoundhaving at least two double carbon-carbon bonds. In some embodiments thecross linker is secondary diamide. In exemplary embodiments, the crossliker comprises at least one A₁. In some embodiment, the cross likerfurther comprises at least one A₂.

In formula I as noted herein above B is haloatom.

As used in the art, the term “halo”, “halo atom” or “halogen” refers toan atom selected from the group consisting of: chlorine, bromine, andiodine and fluorine.

In some embodiments, one or more hydrogens bound to a nitrogen atom inthe crosslinked polymeric are substituted (also termed hereinthroughout: “halogenated”) in each instance, by a halo atom.

In some embodiments, the halogen atom independently selected from thegroup consisting of Cl, Br, I and F. In some embodiments, the halogenatom is Br. In some embodiments, the halogen atom is Cl. In someembodiments, the halogen atom is F. In some embodiments, the halogenatom is I. In some embodiments, the crosslinked polymer is attached toboth Cl and Br atoms. In some embodiments, the crosslinked polymer isattached to both Cl and I atoms. In some embodiments, the crosslinkedpolymer is attached to both Br and I atoms.

In some embodiments, at least one halo atom is bound (also termedhereinthroughout as “attached”) to a nitrogen atom belonging to thesecondary diamide monomeric unit, as described herein. In someembodiments, at least one halo atoms is bound to the nitrogen atombelonging to a primary amide monomeric unit, as described herein.

The total number of the secondary diamide monomers and crosslinkerwithin the crosslinked polymeric backbone is defined herein as “x”; thenumber of the primary amide monomer within the crosslinked polymericbackbone is herein defined as “y”.

The number of the halo atom attached to the crosslinked polymericbackbone is defined as n.

It would be appreciated that x, and y can be controlled as desired byselecting the mol ratio of the respective monomeric units used forforming the crosslinked polymeric backbone, as discussed hereinbelow.

In some embodiments, the sum of x+y, representing the total numbers ofA₁ and A₂, respectively, in a crosslinked polymeric backbone, has avalue of at least e.g., 1, 5, 10, 15, 20, 25, 30, 35, 40, 45, 50, 55,60, 75, 80, 85, 90, 95, 100, including any value therebetween. In someembodiments, x has a value of at least e.g., 1, 5, 10, 15, 20, 25, 30,35, 40, 45, 50, 55, 60, 75, 80, 85, 90, 95, 100, including any valuetherebetween. In some embodiments, y has a value of at least e.g., 1, 5,10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 75, 80, 85, 90, 95, 100,including any value therebetween.

It would be further appreciated that n can be controlled as desired byselecting the halogenation parameters as discussed hereinbelow under“The Process”.

For example n/(x+y) multiplied by 100 may be o, meaning that no haloatom is attached to the crosslinked polymeric backbone.

In some embodiments, n/(x+y) multiplied by 100 maybe e.g. at least e.g.:1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20,30, 40, 50, 60, 70, 75 76, 77, 78, 79, 80, 81, 82, 83, 84, 85, 86, 87,88, 89, 90, 91, 92, 93, 94, 95, 96, 97, 98, 99, 100, 110, 120, 130, 140,150, 160, 170, 180, 190, 200, including any value therebetween.

Hereinthroughout, the terms “nanoparticle”, “nano”, “nanosized”, and anygrammatical derivative thereof, which are used herein interchangeably,describe a particle featuring a size of at least one dimension thereof(e.g., diameter, length) that ranges from about 1 nanometer to 1000nanometers. Hereinthroughout NP(s) designates nanoparticle(s).

In some embodiments, the size of the particles described hereinrepresents an average size of a plurality of nanoparticle composites ornanoparticles.

In some embodiments, the average size of at least e.g., 10%, 20%, 30%,40%, 50%, 60%, 70%, 80%, 90%, 95% of the cross-linked polymers,including any value therebetween, ranges from: about 1 nanometer to 1000nanometers, or, in other embodiments from 1 nm to 500 nm, or, in otherembodiments, from 10 nm to 200 nm, In some embodiments, the average sizeranges from about 1 nanometer to about 300 nanometers. In someembodiments, the average size ranges from about 1 nanometer to about 200nanometers. In some embodiments, the average size ranges from about 1nanometer to about 100 nanometers. In some embodiments, the average sizeranges from about 1 nanometer to 50 nanometers, and in some embodiments,it is lower than 35 nm.

In some embodiments, a plurality of crosslinked polymeric backbones ischaracterized by an average hydrodynamic diameter of less than 50 nmwith a size distribution of that varies within a range of less thane.g., 60%, 50%, 40,%, 30%, 20%, 10%, including any value therebetween.

In some embodiments, plurality of crosslinked polymeric backbones arecharacterized by an average hydrodynamic diameter of less than 30 nmwith a size distribution of that varies within a range of less thane.g., 60%, 50%, 40,%, 30%, 20%, 10%, including any value therebetween.

In some embodiments, the average size of the crosslinked polymer isabout 1 nm, about 2 nm, about 3 nm, about 4 nm, about 5 nm, about 6 nm,about 7 nm, about 8 nm, about 9 nm, about 10 nm, about 11 nm, about 12nm, about 13 nm, about 14 nm, about 15 nm, about 16 nm, about 17 nm,about 18 nm, about 19 nm, about 20 nm, about 21 nm, about 22 nm, about23 nm, about 24 nm, about 25 nm, about 26 nm, about 27 nm, about 28 nm,about 29 nm, about 30 nm, about 31 nm, about 32 nm, about 33 nm, about34 nm, about 35 nm, about 36 nm, about 37 nm, about 38 nm, about 40 nm,about 42 nm, about 44 nm, about 46 nm, about 48 nm, or 50 nm, includingany value therebetween.

As used herein the term average size refers to diameter of thecrosslinked polymer. The term “diameter” is art-recognized and is usedherein to refer to either of the physical diameter (also termed “drydiameter”) or the hydrodynamic diameter. As used herein, the“hydrodynamic diameter” refers to a size determination for thecrosslinked polymer in solution (e.g., aqueous solution) using anytechnique known in the art, e.g., dynamic light scattering (DLS).

As exemplified in the Example section that follows, the dry diameter ofthe crosslinked polymer, as prepared according to some embodiments ofthe invention, may be evaluated using cryo-transmission electronmicroscopy (TEM) imaging. In exemplary embodiments, the dry diameter ofthe crosslinked polymer, as prepared according to some embodiments ofthe invention, is about 5 nm, and the hydrodynamic diameter, asevaluated by DLS is about 27 nm.

The crosslinked polymeric particle(s) can be generally shaped as asphere, a rod, a cylinder, a ribbon, a sponge, and any other shape, orcan be in a form of a cluster of any of these shapes, or can comprises amixture of one or more shapes.

In some embodiments, the composition-of-matter comprises a plurality ofcrosslinked polymeric particles, and at least 10%, 20%, 30%, 40%, 50%,60%, 70%, 80%, 90%, 95%, 98%, 99%, 99.9%, or all of the crosslinkedpolymeric particle are nanosized as described herein, e.g., in shape andaverage size.

In some embodiments, the plurality of crosslinked polymeric particles isin a form of a dry powder. As used herein, “dry powder” refers to apowdered particle that is a finely dispersed solid i.e., not suspendedor dissolved in a propellant, or other liquid.

Any one of the compositions-of-matter described herein, and anyembodiments thereof, including exemplary compositions-of-matter asdescribed herein, can be prepared by any method known if the art forobtaining the crosslinked polymeric particles, including the method asdescribed herein. In some embodiments, the composition-of-matter isprepared by co-polymerizing a plurality of monomers A₁ and A₂ as definedhereinabove. In exemplary embodiments, A₁ is N,N-methylene bisacrylamideand A₂ is methacrylamide.

In some embodiments, the an initial weight ratio of A₁ to A₂ of aboute.g., 1:9, 2:9, 1:4, 1:3, 1:2, 1:1, 6:5, 6:4, including any valuetherebetween is used for said polymerization.

In exemplary embodiments, the polymerization is performed in asurfactant-free dispersion. In some embodiments the dispersion furthercomprises at least one water soluble initiator. Exemplary water solubleinitiators include, but are not limited to, AIBNCO₂H, PPS, H₂O₂, asfurther described and defined hereinbelow, under “The Process”.

In some embodiments, the plurality of crosslinked polymeric backbones isfurther subjected to a step of halogenations. As used herein“halogenations” refers to chlorination, bromination, or iodination, orcombination thereof, as further described herein below, under “TheProcess”. Further embodiments of the composition-of matter are describedhereinbelow.

Substrates and/or Articles:

According to some of any of the embodiments described herein, acomposition according to any one of the respective embodiments, furthercomprises a substrate. In some embodiments a plurality of halogenated ornon-halogenated crosslinked polymeric backbones as described in any ofthe respective embodiments is incorporated in and/or on at least aportion of the substrate. Herein, “halogenated crosslinked polymericbackbones” also refer to crosslinked polymeric backbones capable ofbeing rechargeable with halo atoms, as described hereinbelow.

According to an aspect of some embodiments of the present invention,there is provided a substrate having incorporated in and/or on at leasta portion thereof, crosslinked polymeric backbones as described herein.

According to an aspect of some embodiments of the present inventionthere is provided a substrate having incorporated in and/or on at leasta portion thereof a halogenated crosslinked polymeric backbones asdescribed herein in any of the respective embodiments.

By “a portion thereof” it is meant, for example, a surface or a portionthereof, and/or a body or a portion thereof, of solid or semi-solidsubstrates; or a volume or a part thereof, of liquid, gel, foams andother non-solid substrates.

Substrates of widely different chemical nature can be successfullyutilized for incorporating (e.g., depositing on a surface thereof)crosslinked polymeric backbones thereon, as described herein. By“successfully utilized” it is meant that (i) the halogenated crosslinkedpolymeric backbones successfully form a uniform and homogenously coatingon the substrate's surface; and (ii) the resulting coating impartslong-lasting desired properties (e.g., antimicrobial properties) to thesubstrate's surface.

Substrate usable according to some embodiments of the present inventioncan therefore be hard (rigid) or soft, solid, semi-solid, or liquidsubstrates, and may take a form of a foam, a solution, an emulsion, alotion, a gel, a cream or any mixture thereof.

Substrate usable according to some embodiments of the present inventioncan have, for example, organic or inorganic surfaces, including, but notlimited to, glass surfaces; porcelain surfaces; ceramic surfaces;silicon or organosilicon surfaces, metallic surfaces (e.g., stainlesssteel); mica, polymeric surfaces such as, for example, plastic surfaces,rubbery surfaces, paper, wood, polymer, a metal, carbon, a biopolymer,silicon mineral (rock or glass), surfaces, wool, silk, cotton, hemp,leather, fur, feather, skin, hide, pelt or pelage) surfaces, plasticsurfaces and surfaces comprising or made of polymers such as but notlimited to polypropylene (PP), polycarbonate (PC), polyethylene (PET),high-density polyethylene (HDPE), low-density polyethylene (LDPE),polyester (PE), unplasticized polyvinyl chloride (PVC), andfluoropolymers including but not limited to polytetrafluoroethylene(PTFE, Teflon®); or can comprise or be made of any of the foregoingsubstances, or any mixture thereof.

Alternatively, other portions, or the entire substrate are made of theabove-mentioned materials.

In some embodiments, the substrate incorporating the crosslinked polymeras described herein is or forms a part of an article.

Hence according to an aspect of some embodiments of the presentinvention there is provided an article (e.g., anarticle-of-manufacturing) comprising a substrate incorporating in and/oron at least a portion thereof a composition-of-matter or the crosslinkedpolymer, as described in any one of the respective embodiments herein.

The article can be any article which can benefit from the antimicrobialand/or anti-biofilm formation activities of the halogenated crosslinkedpolymeric backbones.

Exemplary articles include, but are not limited to, medical devices,organic waste processing device, fluidic device, an agricultural device,a package, a sealing article, a fuel container, a water and coolingsystem device and a construction element.

Non-limiting examples of devices which can incorporate the halogenatedcrosslinked polymer, as described herein, beneficially, include tubing,pumps, drain or waste pipes, screw plates, and the like.

In some embodiments, the article is an element used in water treatmentsystems (such as for containing and/or transporting and/or treatingaqueous media or water), devices, containers, filters, tubes, solutionsand gases and the likes.

In some embodiments, the article is an element in organic wastetreatment systems (such as for containing and/or disposing and/ortransporting and/or treating organic waste), devices, containers,filters, tubes, solutions and gases and the likes.

Contaminant Treating Applications:

While studying the activity of the compositions of matter as describedhereinabove, and the activity of compositions-of-matter in whichcrosslinked polymers are deposited on a substrate's surface, asdescribed herein, the present inventors have surprisingly uncovered thatsuch compositions of matter exhibit high and long lasting antifoulingactivity and can therefore be beneficially incorporated in articles ofin which such an activity is desired. By “long lasting antifoulingactivity” it is meant to refer to the ability of thecompositions-of-matter as described hereinthroughout to withstandrepetitive loading cycle of organic based material (e.g., bacteria).Additionaly, or alternatively, it is meant to refer to the ability ofthe compositions-of-matter as described hereinthroughout to maintain itsactivity against organic based contaminant, within less than 30%variation, up to a period of at least six months.

Because wastewater and sludge treatment generally include primary andsecondary treatment, which may only remove a fraction of the pathogenicmicroorganisms, discharge of treated wastewater and sludge represent apotential source of microbial contamination, and, in this respects, thecompositions-of-matter as described hereinthroughout, is of particularbeneficial.

The present process is effective for treating one or more contaminantcomponents, e.g., organic-based components, such as hydrocarbons, and/ororganic-based components. Organic-based contaminant components which maybe treated in the present process can include organic sulfur, inparticular, non-thiophenic sulfur. Examples of organic-based andhydrocarbon-based contaminant components which may be processed inaccordance with the present invention include, but are not limited to,petroleums (crude oils including topped crude oils), organic acids suchas benzoic acid, ketones, aldehydes, aromatic components includingphenols and the like, organic materials containing hetero atoms such asnitrogen, sulfur and halogen, e.g., chloride, and the like, dyes,polymeric materials, including, without limitation polymericcarbohydrate(e.g., polysaccharides), proteins, fatty acids and mixtures thereof.Other contaminants which may be treated in the present process include,for example, and without limitation, materials which are activecomponents in or products of a manufacturing process, such as cyanide orhydrazine, or a process by-product, organic insecticides, herbicides,sewage contamination, and pesticides resulting from soil leaching due tocontinuous water usage in agriculture, e.g., the production of fruitsand vegetables particularly in arid to semi-arid climates.

In one embodiment of the invention, the process comprises contacting thecontaminant component or components with at least one of the halogenatedcrosslinked polymers as described hereinabove so as to provide chemicalmodification of contaminant component or components to provide lessenvironmentally deleterious or more environmentally acceptableaqueous-based materials, preferably in high yields. It is noteworthythat the composition-of-matter and/or the articles as describedhereinabove are used at a concentration which does not providesubstantial adverse environmental effects.

The term “chemical modification” as used herein refers to a change inthe contaminant component or components which change results from thechemical conversion, e.g., chemical reaction, oxidation and/ordegradation and/or alteration of at least one environmentally adverseproperty, of one or more of such contaminant components. Also, thechemical modification may occur with regard to the carbon and/orhydrogen portions of the organic-containing contaminant componentsand/or to the other portions, e.g., such as contained sulfur, nitrogen,phosphate, oxygen, halide, metals or the like, of suchorganic-containing contaminant components.

In addition, such modification can reduce one or more of theenvironmentally objectional characteristics of such contaminantcomponent or components to yield aqueous-based materials, includingprocess water streams and ground water streams having, for example, areduced level of such contaminated component or components.

In some embodiments the composition-of-matter and/or the articles asdescribed hereinthroughout are utilized for self-cleaning coatings. Asused herein, the term “self-cleaning” means the property of a surfacethat generally keeps the surface clean without mechanical force ordetergent to loosen and remove visual detractants.

According to some embodiments of the present invention, thecomposition-of-matter as described hereinthroughout is incorporatedwithin a formulation. In some embodiments, the formulation is used as anantibacterial and/or antifungal cleaner.

Antimicrobial Anti-Biofilm Formation Applications:

According to another aspect of some embodiments of the present inventionthere is provided a method of inhibiting or reducing or retarding theformation of load of a microorganism and/or the formation of a biofilm,in and/or on an article. The method comprises incorporating in and/or onthe article any one of the compositions-of-matter as described herein,including any of the respective embodiments thereof.

As further exemplified in the Examples section that follows, thechlorinated NPs and the articles comprising the same exhibit highcapability to withstand repetitive cycles of bacterial exposure. Thearticle can be any one of the articles described herein.

Such articles, therefore, take advantage of the improved antimicrobialactivity exhibited by the halogenated crosslinked polymer as describedherein.

Herein “antimicrobial activity” is referred to as an ability to inhibit(prevent), reduce or retard bacterial growth, fungal growth, biofilmformation or eradicate living bacterial cells, or their spores, orfungal cells or viruses in a suspension, on a surface or in a moistenvironment.

Herein, inhibiting or reducing or retarding the formation of load of amicroorganism refers to inhibiting reducing or retarding growth ofmicroorganisms and/or eradicating a portion or all of an existingpopulation of microorganisms.

Thus, the halogenated crosslinked polymer as described herein can beused both in reducing the formation of microorganisms on or in anarticle, and in killing microorganisms in or on an article or a livingtissue.

The microorganism can be, for example, a unicellular microorganism(prokaryotes, archaea, bacteria, eukaryotes, protists, fungi, algae,euglena, protozoan, dinoflagellates, apicomplexa, trypanosomes, amoebaeand the likes), or a multicellular microorganism. As used herein, theterms “bacteria”, or “bacterial cells” may refer to either Gram-positivebacteria (e.g., S. aureus) and/or Gram-negative bacteria (e.g., E. coli)and archae, including multi-drug resistant (MDR) bacteria.

In some embodiments of the present invention the composition-of-matterin any embodiment as described hereinthroughout, may be characterized byhigh affinity to a specified bacteria type, species, or genus.Therefore, in some embodiments of the present invention thecomposition-of-matter in any embodiment as described hereinthroughout,the composition-of-matter may be used an effective way for selectivelytargeting bacteria

Herein “anti-biofouling activity” or “antifouling activity” is referredto as an ability to inhibit (prevent), reduce or retard biofilmformation on a substrate's surface.

The term “biofilm”, as used herein, refers to an aggregate of livingcells which are stuck to each other and/or immobilized onto a surface ascolonies. The cells are frequently embedded within a self-secretedmatrix of extracellular polymeric substance (EPS), also referred to as“slime”, which is a polymeric sticky mixture of nucleic acids, proteinsand polysaccharides.

In the context of the present embodiments, the living cells forming abiofilm can be cells of a unicellular microorganism (prokaryotes,archaea, bacteria, eukaryotes, protists, fungi, algae, euglena,protozoan, dinoflagellates, apicomplexa, trypanosomes, amoebae and thelikes), or cells of multicellular organisms in which case the biofilmcan be regarded as a colony of cells (like in the case of theunicellular organisms) or as a lower form of a tissue.

In the context of the present embodiments, the cells are ofmicroorganism origins, and the biofilm is a biofilm of microorganisms,such as bacteria and fungi. The cells of a microorganism growing in abiofilm are physiologically distinct from cells in the “planktonic form”of the same organism, which by contrast, are single-cells that may floator swim in a liquid medium. Biofilms can go through several life-cyclesteps which include initial attachment, irreversible attachment, one ormore maturation stages, and dispersion. The phrases “anti-biofilmformation activity” refers to the capacity of a substance to effect theprevention of formation of a biofilm of bacterial, fungal and/or othercells; and/or to effect a reduction in the rate of buildup of a biofilmof bacterial, fungal and/or other cells, on a surface of a substrate. Insome embodiments, the biofilm is formed of bacterial cells (or from abacterium).

In some embodiments, a biofilm is formed of bacterial cells of bacteriaselected from the group consisting of all Gram-positive andGram-negative bacteria and archae

As demonstrated herein, a composition of matter as described herein hasshown to exhibit anti-biofilm formation (ABF) activity and can thusprevent, retard or reduce the formation of a mass of a biofilm.

In some embodiments of the present invention, the activity of preventingor reducing the formation of a biofilm, may be achieved by a substrateor an article incorporating the halogenated crosslinked polymer, asdescribed herein.

The inhibition or reduction or retardation of formation of a biofilmassumes that the biofilm has not yet been formed, and hence the presenceof the halogenated crosslinked polymer nanoparticles are required alsoin cases where no biofilm is present or detected.

As used herein, the term “preventing” in the context of the formation ofa biofilm, indicates that the formation of a biofilm is essentiallynullified or is reduced by at least 20%, at least 30%, at least 40%, atleast 50%, at least 60%, at least 70%, at least 80%, at least 90%,including any value therebetween, of the appearance of the biofilm in acomparable situation lacking the presence of the halogenated crosslinkedpolymer or a composition of matter containing same. Alternatively,preventing means a reduction to at least 15%, 10% or 5% of theappearance of the biofilm in a comparable situation, lacking thepresence of the halogenated crosslinked polymer or acomposition-of-matter or an article containing same. Methods fordetermining a level of appearance of a biofilm are known in the art.

As used herein, the term “preventing” in the context of antimicrobial,indicates that the growth rate of the microorganism cells is essentiallynullified or is reduced by at least 20%, at least 30%, at least 40%, atleast 50%, at least 60%, at least 70%, at least 80%, at least 90%,including any value therebetween, of the appearance of the microorganismin a comparable situation lacking the presence of the halogenatedcrosslinked polymer or a composition of matter containing same.Alternatively, preventing means a reduction to at least 15%, 10% or 5%of the appearance of the microorganism cells in a comparable situationlacking the presence of the halogenated crosslinked polymer or acomposition of matter containing same. Methods for determining a levelof appearance of a microorganism cells are known in the art.

In some embodiments there is provided an article which comprises thecomposition of matter incorporated in and/or on a substrate.

Compositions of matter as described herein can be incorporated withinany of the articles of manufacturing, during manufacture of any of thearticle described herein.

The substrates presented herein can be used to modify any industrial orclinical surface to prevent bacterial colonization and biofilmformation.

The Process:

The present inventors have designed and successfully practiced novelprocesses for preparing a uniform cross-linked polymamide nanopaticlesas described hereinabove. It is to note that synthesizing such acontrolled size of the polymer is subjected to various limitations,imposed by a e.g., different tendency of the monomers to disperse in thesolution, complicated desired structural features that are required foroptimal size, uniformity, and performance of the crosslinked polymer,incompatibility of the reactants, initiators and the like. Hence,devising a process that overcomes these limitations and is designed toobtain a uniform cross-linked polyamide nanoparticles that exhibits atleast a reasonable performance is highly advantageous.

Hence, according to another aspect of embodiments of the invention thereis provided a process of synthesizing the composition-of-matterdescribed herein, the process comprising: co-polymerizing a plurality ofsaid monomers A₁ and A₂, the co-polymerizing comprising dispersing saidmonomers in a weight ratio of A₁/A₂ that ranges from about 1:9 to about6:4 in a surfactant-free aqueous phase comprising an initiator, tothereby obtain a polymeric material characterized by an averagehydrodynamic diameter of at least one dimension thereof of less than 500nm with a size distribution that varies within a range of less than 20%.

The polymerization of various monomeric units can be effected by anypolymerization method known in the art, e.g., using suitablepolymerization initiators and optionally chain transfer agents. Suchsuitable polymerization initiators and chain transfer agents can bereadily identified by a person skilled in the art.

As demonstrated in the Examples section that follows, the polymerizationcan be performed via a radical polymerization methodology in an aqueoussolution.

The term “radical polymerization” or “free radical polymerization”refers to a method of polymerization by which a polymer is formed fromthe successive addition of free radical building blocks. Free radicalscan be formed via a number of different mechanisms usually involvingseparate initiator molecules. Since the radical polymerization initiatorcan generate a radical by abstracting hydrogen from a carbon-hydrogenbond, when it is used in combination with an organic material such as apolyolefin a chemical bond can be formed. Following creation of freeradical monomeric units, polymer chains grow rapidly with successiveaddition of building blocks onto free radical sites.

As a radical polymerization initiator for initiated polymerization orredox initiated polymerization, the following exemplary water solubleradical polymerization initiators may be used, without being limitedthereto, singly or in a combination of two or more types: peroxides suchas ammonium persulfate, potassium persulfate, sodium persulfate,hydrogen peroxide, benzoyl peroxide, cumene hydroperoxide, or di-t-butylperoxide; a redox initiator that is a combination of the above-mentionedperoxide and a reducing agent such as a sulfite, a bisulfite,thiosulfate, formamidinesulfinic acid, or ascorbic acid; or an azo-basedradical polymerization initiator, such as, without limitation,2,2′-azobis(2-amidinopropane) (AIBN), AIBNCOOH, and2,2′-azobis(2-amidinopropane), and potassium persulfate (PPS). Inexemplary embodiments, the initiator is selected from the groupconsisting of: PPS and AIBN.

As described hereinabove, it is to be understood that a polymerizationprocess utilizing monomer having a functional group that can form acrosslinked structure.

From the viewpoint of ease of incorporation of the crosslinked structureas described hereinabove under “The Compositions-of-matter”, the methodin which a polymerization reaction is carried out using in combination acrosslinking agent (monomer) having at least two polymerizable doublecarbon-carbon bonds. Similar crosslinking reaction may be caused byheating at the same time as radical polymerization.

It is to be understood that other radical polymerization methodology canbe applied, such as, without limitation, living radical polymerization.

By “living polymerization” it is meant to refer to a form of chaingrowth polymerization where the ability of a growing polymer chain toterminate has been removed. Living radical polymerization is a type ofliving polymerization where the active polymer chain end is a freeradical.

Several methodologies of living radical polymerization are known in theart and are conceivable to be applied in the context of the presentinvention, including, without limitation, reversible-deactivationpolymerization, catalytic chain transfer, cobalt mediated radicalpolymerization, iniferter polymerization, stable free radical mediatedpolymerization, atom transfer radical polymerization, reversibleaddition fragmentation chain transfer (RAFT) polymerization,iodine-transfer polymerization (ITP), selenium-centered radical-mediatedpolymerization, telluride-mediated polymerization (TERP), andstibine-mediated polymerization.

As described hereinthroughout, in some of any of the embodiments, thepolymerization process is affected in an aqueous solution comprising themixture of monomeric units A₂ and A₁ as defined herein above, under “TheComposition of Matter” and an initiator.

In exemplary embodiments, the monomeric units (or monomers) are MAA andMBAA. In some embodiments the ratio between A₂ and A₁ prior to thepolymerization thereof is e.g., 1:1, 1:2, 1:3:1:4, 1:5, 1:6, 1:7, 1:8,1:9, 1:10, 2:1, 3:1, 4:1, 5:1, 6:1, 7:1, 8:1, 9:1, 10:1, including anyvalue therebetween. As described in the Examples section that follows,the nanoparticle size of the crosslinked polymer is affected by theinitial weight ratio of A₁ and A₂ in the solution.

In exemplary embodiments, the steady ratio of MAA and MBAA are 55%MAA:45% MBAA. In exemplary embodiments, the total concentration (% w/v)of the monomers in the solution is e.g., 1%, 2%, 3%, 4%, 5%, includingany value therebetween. As exemplified in the Examples section thatfollows, the hydrodynamic diameter of the formed P(MAA-MBAA) isincreased with increasing the total concentration of the monomers.

As described in the Example section that follows, the initiator type(e.g., PPS and AIBN) and the concentration thereof may affect on thehydrodynamic size and size distribution of the formed crosslinkedpolymeric nanoparticles.

In exemplary embodiments, the concentration of the initiator, e.g., PPS,or AIBN, is e.g., 1%, 2%, 3%, 4%, 5%, 6%, 7%, 8%, 9%, 10%, including anyvalue therebetween.

In some embodiments, the size and the polymerization yield of thecrosslinked polymer is affected by the temperature. In some embodimentsthe mixture or solution is maintained at a temperature that ranges from10° C. to 100° C., during the polymerization procedure. In someembodiments the mixture or solution is maintained at temperature thatranges from 40° C. to 90° C., or from 45° C. to 95° C., or from 60° C.to 100° C.

In exemplary embodiments the mixture or solution is maintained at about90° C.

In some embodiments the size and the diameter of the crosslinked polymeris affected by duration (time) of polymerization process.

In some embodiments, the duration of polymerization process is at least1 minute. In some embodiments, the duration of polymerization process isat least 30 seconds, at least 1 minute, at least 2 minutes, at least 3minutes, at least 5 minutes, at least 10 minutes, at least 15 minutes,at least 20 minutes, at least 25 minutes, at least 30 minutes, at least35 minutes, at least 40 minutes, at least 45 minutes, or at least 50minutes. In exemplary embodiments, the duration of polymerizationprocess is at least 1 minute, e.g., 1 min, 5 minutes or 30 minutes. Eachpossibility represents a separate embodiment of the invention.

In some embodiments, the crosslinked polymer as describedhereinthroughout is at least partially halogenated. By “at leastpartially halogenated” it is meant that at least 1%, 2%, 5%, 10%, 15%,20%, 30%, 40%, 50%, 60%, 70%, 80%, 90%, 99%, of the hydrogens bound to anitrogen atom in the crosslinked polymeric are substituted by halogenatom, as defined and described hereinabove, under “TheComposition-of-matter”.

The halogenations process may be carried out during the polymerizationprocess or after the polymerization process, i.e. on the crosslinkedpolymers.

In exemplary embodiments, the halogenation (e.g., chlorination) processis applied on the P(MAA-MBAA) particles (i.e. after the polymericprocess) of 20-50 nm, 25-35 nm, or about 27 nm diameter, as detailed inthe Examples section that follows.

In some embodiments, the halogenation is applied by addition of a halidesource to a solution comprising the crosslinked polymers, selected from,but not limited to, one or more salts of a material selected from thegroup consisting of: di-X-isocyanurate, hypo-halite, N X-succinimide, orhypo-halite, wherein said halite and X each are selected from the groupconsisting of: Cl, I or Br. In some embodiments, the salt is selectedfrom sodium or calcium salts. In exemplary embodiments the halogenationis chlorination being performed using one or more chlorine sourcereagents selected from, for example and without limitation, hypochlorite(NaOCl), and dichlorocyanuric acid (DCCA).

In some embodiments, the halogenation is affected by the concentration(% w/v) of the halide source. By “halogenation is affected” it is meantto refer to the percent of the hydrogen atoms bound to a nitrogen atomin the crosslinked polymer being substituted by the halogen atom.

In some embodiments, the concentration of the halide source is e.g.,0.001%, 0.005%, 0.01%, 0.05, 0.1%, 0.5%, 1%, 1.5%, 2%, 2.5%, 3%, 3.5%,4%, 5%, 10%, 20%, including any value therebetween, of a solutioncomprising the crosslinked polymer.

In some embodiments, the halogenation is affected by the haloginationtime. In exemplary embodiments, as further described in the Examplessection that follows, the halogination time ranges e.g., from about 1minute to about 150 minutes, from about 10 minutes to about 100 minutes,from about 20 minutes to about 90 minutes, from about 30 minutes toabout 80 minutes, or from about 40 minutes to about 60 minutes.

In some embodiments, the halogenation is affected by the halogenationtemperature. In exemplary embodiments, as further described in theExamples section that follows, the halogenations process was carried outat temperature that ranges from 30° C. to 80° C., following thepolymerization procedure. In some embodiments the halogenation iscarried out at temperature that ranges from 20° C. to 100° C., or from45° C. to 75° C., or from 50° C. to 70° C.

In some embodiments, the halogenated crosslinked polymer may bedehalogeneted. By “dehalogeneted”, or any grammatical derivativethereof, it is meant that the % of the halogen atom in the crosslinkedpolymer is reduced. Dehalogenation may be spontaneous over time, uponcontact with organic-based material, e.g., bacteria, or initiated byexposure to U.V. radiation.

As exemplified in the Examples section that follows, at least e.g. 85%,and even 95% of the halogen atom in the crosslinked polymer aremaintained (i.e. remains not dehalogenated) over a time of at least onemonth, 2 months, 3 months, 4 months, 5 months, 6 months, 7 months, 8months, 9 months, 10 months. 11 months, 12 months, 13 months, 14 months,15 months.

In some embodiments, the “dehalogeneted” atoms may be rechargeable, i.e.rehalogenated, by using any halide source as described hereinabove.

In some embodiments, several cycles (also termed herein “loading cycle”)e.g., at least 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 15, 20, 25, 30, 35, 40,50, 60, 70, of dehalogenetion-rehalogenation may be applied on thecomposition-of mater or article as described hereinthroughout.

General

It is expected that during the life of a patent maturing from thisapplication many relevant nanosized crosslinked polyamide will bedeveloped and the scope of the term crosslinked polyamide is intended toinclude all such new technologies a priori.

As used herein the term “about” refers to ±10%.

The terms “comprises”, “comprising”, “includes”, “including”, “having”and their conjugates mean “including but not limited to”. The term“consisting of” means “including and limited to”. The term “consistingessentially of” means that the composition, method or structure mayinclude additional ingredients, steps and/or parts, but only if theadditional ingredients, steps and/or parts do not materially alter thebasic and novel characteristics of the claimed composition, method orstructure.

The word “exemplary” is used herein to mean “serving as an example,instance or illustration”. Any embodiment described as “exemplary” isnot necessarily to be construed as preferred or advantageous over otherembodiments and/or to exclude the incorporation of features from otherembodiments.

The word “optionally” is used herein to mean “is provided in someembodiments and not provided in other embodiments”. Any particularembodiment of the invention may include a plurality of “optional”features unless such features conflict.

As used herein, the singular form “a”, “an” and “the” include pluralreferences unless the context clearly dictates otherwise. For example,the term “a compound” or “at least one compound” may include a pluralityof compounds, including mixtures thereof.

Throughout this application, various embodiments of this invention maybe presented in a range format. It should be understood that thedescription in range format is merely for convenience and brevity andshould not be construed as an inflexible limitation on the scope of theinvention. Accordingly, the description of a range should be consideredto have specifically disclosed all the possible subranges as well asindividual numerical values within that range. For example, descriptionof a range such as from 1 to 6 should be considered to have specificallydisclosed subranges such as from 1 to 3, from 1 to 4, from 1 to 5, from2 to 4, from 2 to 6, from 3 to 6 etc., as well as individual numberswithin that range, for example, 1, 2, 3, 4, 5, and 6. This appliesregardless of the breadth of the range.

Whenever a numerical range is indicated herein, it is meant to includeany cited numeral (fractional or integral) within the indicated range.The phrases “ranging/ranges between” a first indicate number and asecond indicate number and “ranging/ranges from” a first indicate number“to” a second indicate number are used herein interchangeably and aremeant to include the first and second indicated numbers and all thefractional and integral numerals therebetween.

As used herein the term “method” refers to manners, means, techniquesand procedures for accomplishing a given task including, but not limitedto, those manners, means, techniques and procedures either known to, orreadily developed from known manners, means, techniques and proceduresby practitioners of the chemical, pharmacological, biological,biochemical and medical arts.

As used herein, the term “treating” includes abrogating, substantiallyinhibiting, slowing or reversing the progression of a condition,substantially ameliorating clinical or aesthetical symptoms of acondition or substantially preventing the appearance of clinical oraesthetical symptoms of a condition.

In those instances where a convention analogous to “at least one of A,B, and C, etc.” is used, in general such a construction is intended inthe sense one having skill in the art would understand the convention(e.g., “a system having at least one of A, B, and C” would include butnot be limited to systems that have A alone, B alone, C alone, A and Btogether, A and C together, B and C together, and/or A, B, and Ctogether, etc.). In those instances where a convention analogous to “atleast one of A, B, or C, etc.” is used, in general such a constructionis intended in the sense one having skill in the art would understandthe convention (e.g., “a system having at least one of A, B, or C” wouldinclude but not be limited to systems that have A alone, B alone, Calone, A and B together, A and C together, B and C together, and/or A,B, and C together, etc.). It will be further understood by those withinthe art that virtually any disjunctive word and/or phrase presenting twoor more alternative terms, whether in the description, claims, ordrawings, should be understood to contemplate the possibilities ofincluding one of the terms, either of the terms, or both terms. Forexample, the phrase “A or B” will be understood to include thepossibilities of “A” or “B” or “A and B.”

It is appreciated that certain features of the invention, which are, forclarity, described in the context of separate embodiments, may also beprovided in combination in a single embodiment. Conversely, variousfeatures of the invention, which are, for brevity, described in thecontext of a single embodiment, may also be provided separately or inany suitable subcombination or as suitable in any other describedembodiment of the invention. Certain features described in the contextof various embodiments are not to be considered essential features ofthose embodiments, unless the embodiment is inoperative without thoseelements.

Various embodiments and aspects of the present invention as delineatedhereinabove and as claimed in the claims section below find experimentalsupport in the following examples.

EXAMPLES

Reference is now made to the following examples, which together with theabove descriptions illustrate some embodiments of the invention in a nonlimiting fashion.

Example 1 Material and Methods Materials

All chemicals were of analytical-grade and used with no furtherpurification.

MAA, MBAA sodium hypochlorite (4%), potassium persulfate (PPS)dichlorocyanuric acid (DCCA) and 2,20-Azobisisobutyronitrile (AIBN) werepurchased from Sigma Aldrich (Rehovot, Israel); sodium iodide waspurchased from Strem Chemicals (Newburyport, Mass., USA); acetic acidwas purchased from Fisher Scientific (Loughborough, UK);sodiumthiosulfate (0.01 N) was purchased from Acros Organics (Geel,Belgium); and water was purified by passing deionized water through anElgastat Spectrum reverse osmosis system (Elga LTD, High Wycombe, UK).

Instruments

Attenuated total reflectance (ATR) analysis was performed with BrukerPlatinum ATR QuickSnap™ sampling modules A220/D-01. The samples wereanalyzed over 100 scans at a 4 cm⁻¹ resolution. The hydrodynamicdiameter and size distribution of the particles dispersed in water weremeasured at room temperature with a particle analyzer, model NANOPHOX(Sympatec GmbH, Germany). The size and size distribution of the driedparticles were measured with a cryogenic transmission electronmicroscope (cryo-TEM). For this purpose, a small droplet of an aqueousdispersion of the nanoparticles was placed on a perforated carbon filmsupported on a TEM copper grid held by tweezers. The drop was blottedwith a piece of filter paper, resulting in the formation of thin filmsof 100 to 300 nm thickness within the micropores of the carbon-coatedlace-like polymer layer supported on the grid. The specimen wassubsequently plunged into a reservoir of liquid ethane cooled by liquidnitrogen to ensure its vitrification (rapid freezing) and to prevent icecrystal formation. The vitrified specimen was transferred under liquidnitrogen and mounted on a cryogenic sample holder cooled to −170° C. Allsamples were observed under low-dose conditions. Vitrified samples wereexamined in an FEI T12 G2 Cryo-TEM operating at 120 kV and equipped withan Oxford CT-3500 cryo-holder system. Images were recorded with a GatanUS1000 high-resolution cooled CCD camera and processed withDigitalMicrograph version 3.3.1 software. The rampshaped optical densitygradients in the background were digitally corrected. The thermalbehavior of the P(MAA-MBAA) and P(MAA-MBAA)-Cl nanoparticles wasmeasured by thermogravimetric analysis (TGA) (TGA/DSC 1 STAR^(e) System,Mettler Toledo, Switzerland). This analysis was performed withapproximately 10 mg of dried sample under a nitrogen atmosphere (200mL/min) at a heating rate of 10° C. per min.

Example 2 Polymer Synthesis

Preparation of the Cross-Linked P(MAA-MBAA) Nanoparticles

In exemplary procedures, P(MAA-MBAA) nanoparticles of hydrodynamic sizesranging from 18±2 to 460±60 nm were formed by surfactant-free dispersioncopolymerization of the monomers MAA and MBAA in water as a continuousphase. In exemplary procedures, P(MAA-MBAA) nanoparticles of 27±3 nmhydrodynamic diameter were formed by dissolution of 4.4 g of MAA, 3.6 gof MBAA (2% w/v total monomers), and 240 mg of PPS in 400 mL ofdistilled water. The 1 L round-bottom flask containing this solution wasstirred with a mechanical stirrer (200 rpm) at 100° C. for 1 h. The MAAand MBAA residues were subsequently removed from the nanoparticleaqueous dispersion by extensive dialysis against water. The driedP(MAA-MBAA) nanoparticles were obtained by lyophilization. FIG. 1presents a schematic illustration of the synthesis process.

Effect of Various Parameters on the Characterization of the Cross-LinkedP(MAA-MBAA) Nanoparticles:

In further exemplary procedures, as detailed in the Results section thatfollows, the following parameters were tested in respect to thenanometric size and/or the size distribution of the P(MAA-MBAA): totalmonomer concentration; effect of the initiator type and concentration;the weight ratio [MBAA]/[MAA]; polymerization temperature;polymerization duration time.

Results

General Characterization:

FTIR spectra were recorded to verify the polymerization process andhalogenation of the P(MAA-MBAA) nanoparticles. FIG. 2 presents the IRspectrum of the MAA monomer (A) and P(MAA-MBAA) polymeric nanoparticlesbefore (B) and after (C) the chlorination process. The interpretation ofthe MAA monomer spectrum is known from the art and includes peaks at 930cm⁻¹ (corresponding to the stretching of the C—H bonds on CH₂═C), at1,244 cm⁻¹ (corresponding to the stretching of C—N bonds), at 1,603 cm⁻¹(corresponding to the conjugated double bond vibration), at 1,666 cm⁻¹(corresponding to the carbonyl vibration (amide) and N—H bend (amide)),and at 3,195 and 3,395 cm⁻¹ (corresponding to the symmetric andasymmetric stretching of NH₂, respectively). The IR spectrum of thecross-linker monomer MBAA is similar to that of MAA because thesemonomers contain similar bond types. FIG. 2B, which represents theP(MAA-MBAA) polymeric nanoparticles, illustrates that the peaksattributed to the C═C bond at 1,603 and the stretching of the C—H bondson CH₂═C at 933 cm¹ both disappear. This result indicates that thepolymeric particles are indeed free of the monomeric moiety. Thebroadening of the existing peaks in the polymeric nanoparticles (FIG.2B) relative to the monomer units (FIG. 2A) is also expected. FIG. 2C,representing the P(MAA-MBAA)-Cl polymeric nanoparticles, illustrates thesame peaks as in FIG. 2B except for the peak at 3,195 cm⁻¹, which hasnearly disappeared and is replaced by a new peak at 820 cm⁻¹corresponding to the newly formed N—Cl bond. The C—N peak at 1,230 cm⁻¹corresponding to the chlorinated polymeric nanoparticles (FIG. 2C) issignificantly larger than that belonging to the non-chlorinatednanoparticles (FIG. 2B). It is assumed that the substitution of C—N—Hfor C—N—Cl shifted the corresponding peak from 1,244 to 1,230 cm⁻¹ andincreased the intensity of the C—N vibrational bond.

TGA was next performed for both P(MAA-MBAA) and P(MAA-MBAA)-Cl. As shownin FIG. 3, the 5% weight loss near 100° C. for both particles is likelydue to water evaporation. The TGA thermogram of the P(MAA-MBAA)nanoparticles indicates a dramatic weight loss (75%) in the range of295-450° C. due to polymer decomposition. The P(MAA-MBAA)-Clnanoparticles display approximately 80% total weight loss from 200 to455° C. with two main decomposition slopes. The first slope between 200°C. and 320° C. demonstrates a 15% weight loss, attributed primarily toN—Cl decomposition (Cl release). The second slope between 320° C. and450° C. exhibits a 55% weight loss, attributed to polymer decomposition.FIG. 3 also indicates the earlier decomposition of the chlorinatedparticles, likely due to the loss of mechanical strength as aconsequence of the chlorination process.

The evaluation of the size of P(MAA-MBAA) nanoparticles was performedusing both cryo-TEM (FIG. 4A) and dynamic light scattering (DLS) (FIG.4B). As demonstrated in FIG. 4, a significant gap exists between thehydrodynamic and dry diameters. The hydrodynamic diameter and sizedistribution of the P(MAA-MBAA) nanoparticles in the aqueous phase were27±3 nm, whereas the dry diameter and size distribution determined fromthe cryo-TEM image (black dots) were 5±2 nm. The difference between thedry and hydrodynamic diameters of these particles is likely due to theirhydrophilic nature. When dispersed in an aqueous phase, these particlesare likely to contain a substantial amount of absorbed and surfaceadsorbed water, which increases their diameter relative to the driedparticles.

Effect of Various Parameters on the Characterization of the Cross-LinkedP(MAA-MBAA) Nanoparticles:

Total Monomer Concentration:

The effect of the monomers (MAA and MBAA) (at a steady ratio of 55% MAAand 45% MBAA but with different total concentrations) on thehydrodynamic size and size distribution of the produced P(MAA-MBAA)nanoparticles is shown in FIG. 5. Without being bound by any particulartheory, it is assumed that the system is sensitive in view of the factthat a final monomer concentration greater than 3% resulted inaggregated nanoparticles, whereas no nanoparticles were detected at aconcentration lower than 1%. In this range, e.g., when the concentrationof the MAA and MBAA was increased from 1% to 2% and 3% (w/v), thehydrodynamic diameter and size distribution of the formed P(MAA-MBAA)nanoparticles increased from 18±2 nm to 72±7 nm and 331±43 nm,respectively. Without being bound by any particular theory, the increasein the average diameter of the formed P(MAA-MBAA) nanoparticles can beexplained by the effect of the monomer concentrations on the dispersionpolymerization mechanism. A greater monomer concentration in the aqueouscontinuous phase led to longer oligoradicals before termination,resulting in an increase in the average diameter.

Initiator Type:

The effect of the initiator type (PPS and AIBN) and concentration on thehydrodynamic size and size distribution of the formed P(MAA-MBAA)nanoparticles was examined. As shown in FIG. 6, the P(MAA-MBAA)nanoparticles display a moderate increase in the hydrodynamic diameterand size distribution correlated with an increase in the concentrationof the PPS initiator (in the range of 1% to 7%). For example, in thepresence of 2%, 3%, and 7% PPS, the nanoparticle size and sizedistribution increased from 32±4 nm to 69±7 nm and 81±10 nm,respectively. These data are compared with that of AIBN, which indicatedhigher diameters in the same concentration range with a similartendency, e.g., in the presence of 2%, 3%, and 7%, the nanoparticle sizeincreased from 46±5 nm to 164±17 nm and 264±27 nm, respectively. Withoutbeing bound by any particular theory, it is assumed that increasing theinitiator concentration causes an increase in the instantaneousconcentration of the oligomeric radicals, which in turn increases therate of association of the oligomers of the unstable nuclei to formlarger permanent particle nuclei and thus larger final particle sizes.The difference between P(MAA-MBAA) nanoparticle diameters if preparedwith PPS or AIBN can be explained by the difference in the dissociationconstant (K_(d)). The K_(d) of AIBN is 9.0×10⁻⁵ (80° C. in water), whichis higher than the K_(d) of PPS, which is 6.9×10⁻⁵ (80° C. in water).The higher decomposition rate of AIBN increases the instantaneousconcentration of the oligomeric radicals, resulting in an increasedaverage diameter of the obtained nanoparticles, as mentioned previously.

Effect of the Weight Ratio [MBAA]/[MAA] on Nanoparticle Size:

The MAA was polymerized with MBAA by dispersion co-polymerization inwater as a continuous phase to obtain nanoparticles rather than solublepolymer, which was accomplished by holding the total monomer (MAA+MBAA)weight % constant at 2% while the weight ratio between the two monomers([MBAA]/[MAA]) was varied from 1/9 to 6/4. Increasing this ratio above6/4 (e.g., to 7/3) resulted in the formation of severely agglomeratedparticles. FIG. 7 presents the effect of the weight ratio of[MBAA]/[MAA] on the diameter and size distribution of the formedP(MA-MBAA) nanoparticles. The results suggest that the diameter and sizedistribution increase with increases in the [MBAA]/[MAA] weight ratio.For example, when this ratio was increased from 0.11 to 0.43 and 0.82,the average size and size distribution increased from 10±1 nm to 19±2 nmand 71±8 nm, respectively. This behavior was surprising because it isexpected to obtain more compact nanoparticles as the content of thecross-linked points in the polymer increased. Without being bound by anyparticular theory, this behavior may be explained by the fact thatincreasing the hydrophilic properties of the obtained P(MAA-MBAA)nanoparticles (MBAA is more hydrophilic than MAA) leads to an increasedamount of absorbed and surface-adsorbed water molecules, resulting in anincreased hydrodynamic nanoparticle size.

Effect of the Polymerization Temperature on Nanoparticle Size:

During the course of the current research, the polymerizationtemperature was observed to be an effective parameter to control thesize of the obtained nanoparticles. FIGS. 8A-B present the effect ofpolymerization temperatures between 60° C. and 100° C. on the size andsize distribution (A) and on the polymerization yield (B) of the formedP(MAA-MBAA) nanoparticles.

FIG. 8A demonstrates that increasing the polymerization temperatureleads to a sharp decline in the particle diameter and diameterdistribution, from 331±48 nm at 60° C. to 28±3 nm at 100° C. Similarresults, indicating a decrease in the polymeric particle diameter withincreasing temperature, have been reported by several groups fordispersion polymerization. However, a few research groups have reportedthe opposite trend (Bamnolker H, et al., J. Polym. Sci. 1996; 34:1857.Harding I H. Colloid Polym. Sci. 1985; 263,58) and suggested thatincreasing the temperature leads to increasing initiator decomposition,which causes a higher concentration of “activated initiator” and leadsto increases in the polymerization rate and particle size. Theexplanation for the opposite trend, i.e., a size decrease as a result oftemperature increase, is that the high temperature leads to increasedconcentration of the decomposed initiator, which may cause the formationof many nuclei such that each nucleus becomes smaller than what observedat lower temperature.

FIG. 8B demonstrates that the polymerization yield between 60° C. and90° C. is similar, approximately 90%. At 100° C., the polymerizationyield declined slightly to 80%, likely due to a higher decompositionrate of the initiator, which may cause side reactions and/or earlytermination and lower polymerization yield.

Kinetics of Polymerization:

The effect of the polymerization duration time on the diameter and sizedistribution (FIG. 9A) and polymerization yield (FIG. 9B) of the formedP(MAA-MBAA) nanoparticles prepared was examined. The kinetics werestudied at 100° C. because the smallest nanoparticles with the narrowersize distribution of 28±3 nm were obtained at this temperature, asillustrated in FIGS. 8A-B. FIG. 9 illustrates that after 1, 5, and 30min, the size increased from 16±2 nm to 24±3 nm and 27±3 nm,respectively, and the yield increased from 31% to 69% and 96%,respectively. After 30 min and up to 3 h, the size and yield ofP(MAA-MBAA) nanoparticle formation did not vary significantly becausethe polymerization process was nearly complete after 30 min.

Example 3 Chlorination of the P(MMA-MBAA) Nanoparticles

Chlorination of the P(MAA-MBAA) Nanoparticles:

Following the synthesis of the optimal P(MAA-MBAA) nanoparticles,P(MAA-MBAA) nanoparticles of 27±3 nm hydrodynamic diameter were used toinvestigate the effect of varying the chlorination process parameters asfollows:

Sodium hypochlorite aqueous solution (5 mL, 4% w/v) was added to anaqueous dispersion of the P(MAA-MBAA) nanoparticles (5 mL, 15 mg/mL),which was shaken at room temperature for 1 hour. Excess sodiumhypochlorite was removed from the P(MAA-MBAA)-Cl nanoparticle dispersionby extensive dialysis against water. The bound-Cl content of theP(MAA-MBAA)-Cl nanoparticles was determined by iodometric/thiosulfatetitration according to the art using the following expression:

${{Cl}^{+}({mM})} = \frac{N \times V \times 1000}{2}$where N is the normality (equiv/L) and V is the volume (L) of thetitrated sodium thiosulfate solution.

In further exemplary procedures, as detailed in the Results section thatfollows, the following chlorination parameters were tested in respectsto the Cl content: NaOCl concentration, chlorination time, andchlorination temperature.

In exemplary procedures, other halogens were used, and the NPs weresuspended in sodium hydroxide solution and the halogen (bromine oriodine) was added gradually until neutralization to pH 7. Excess sodiumhypochlorite/hypobromite/hypoiodite was removed from the halogenatedP(MAA-MBAA) NPs dispersion by extensive dialysis against water. Thebound-halogen (Br or I) content of the halogenated P(MAA-MBAA) NPs wasdetermined either by adding e.g., sodium iodide and measuring the formedcolor spectrophotometrically at 292 nm and 350 nm or byiodometric/thiosulfate titration.

For determining the I content on the P(MAA-MBAA)-I NPs, analyticalchemical elements was conducted.

Effect of the Chlorination Parameters

Effect of NaOCl Concentration on the Cl Content of the P(MAA-MBAA)-ClNanoparticles:

To characterize the effect of sodium hypochlorite (NaOCl) concentrationon the Cl content of the P(MAA-MBAA)-Cl nanoparticles, increasingconcentrations of NaOCl was conducted as presented in FIG. 10. Thisfigure illustrates that, increasing the NaOCl concentration leads to anincrease in the bound Cl loading of the nanoparticles. For example, inthe presence of 0.8%, 2%, and 3.2% NaOCl, the bound Cl content of theP(MAA-MBAA)-Cl nanoparticles increased from 20.8 mM to 41.4 mM and 67.5mM, respectively. The effect of NaOCl concentrations greater than 3.2%on the bound Cl content could not be measured due to the significantdamage that occurred to the dialysis membranes under these conditions.

Effect of the Chlorination Time on the Cl Content of the P(MAA-MBAA)-ClNanoparticles:

the effect of the chlorination time on the Cl content of theP(MAA-MBAA)-Cl nanoparticles aqueous dispersion was tested asdemonstrated in FIG. 11. The presented trend illustrates that increasingthe chlorination duration from 5 min to 120 min leads to an active Clcontent increase from 20.7±0.25 mM to 30.4±0.3 mM. The main chargingincrease occurs within the first 30 min, followed by milder increaseover the next 120 min. For example, the bound Cl content evaluated after30 min of chlorination was 26.4±0.3 mM, whereas the extension of thechlorination process to 120 min yielded a Cl content of only 30.4±0.3mM.

Effect of Chlorination Temperature on the Cl Content of theP(MAA-MBAA)-Cl Nanoparticles:

The chlorination process was carried out at three different temperaturesof 30° C., 40° C., and 60° C. for 1 h. FIG. 12 illustrates the effect ofthe chlorination temperature on the Cl content of the chlorinatedP(MAA-MBAA) nanoparticles at pH 7. Increasing the chlorinationtemperature from 30° C. to 40° C. and 60° C. leads to an increase of thebound Cl content from 28±2 mM to 32±0.9 mM and 50±4.9 mM, respectively.Increasing the temperature increases the reactivity of the sodiumhypochlorite, leading thereby to increased chlorination.

Extent of Cl Release and Rechargeability of the P(MAA-MBAA)-ClNanoparticles' Aqueous Dispersion Irradiated by Laboratory or UV Light:

In exemplary procedures, the stability and rechargeability of the boundCl of the P(MAA-MBAA)-Cl nanoparticles dispersed in water (20 mL, 4mg/mL) were evaluated by exposure to laboratory or UVA (365 nm) light,as described in hereinabove. FIG. 13 illustrates the change over time ofthe % Cl of the P(MAA-MBAA)-Cl nanoparticle aqueous dispersion storedunder laboratory light conditions. The results indicate a relativelyhigh stability of the N—Cl bond. Storing the chlorinated nanoparticlesunder laboratory light conditions for four months and for one yearresults in the presence of 95% and 85% of the initial bound Cl,respectively. Following a Cl recharging process, as described in theexperimental section, the bound Cl content returned to its initial valueeven after one year of storage under laboratory light conditions (FIG.13). It is assumed that the recharging process changed the N—H bonds ofthe co-polymeric nanoparticles to N—Cl bonds such that the concentrationof the N—Cl groups returned to that of the initial concentration. Asimilar study by Worley et al. reported on the loss of approximately 80%bound Cl within four weeks of N-halamine silane polymer coatings oncotton fabric stored in laboratory light conditions. This result mayindicate that the N—Cl bonds of the P(MAA-MBAA)-Cl are more stable thanthose of the N-halamine silane polymers used by Worley et al. (ColloidSurf A 2009; 345).

In additional exemplary procedures, the stability and rechargeability ofthe bound Cl of the P(MAA-MBAA)-Cl nanoparticles irradiated with UVAover 42 days were examined (FIG. 14). A significant acceleration of thebound Cl loss due to the UVA irradiation was observed. For example,during the 42 days of UVA irradiation, the loss of bound Cl was 91%,whereas the loss of bound Cl for nanoparticles stored under laboratorylight conditions was less than 2%. In addition, FIG. 14 illustrates thatthe rechlorination of the UVA-irradiated nanoparticles was onlypartially successful, e.g., the % bound Cl after 42 days of UVAirradiation returned from 9% to 40% of its initial value after therechlorination process. These results suggest that the UVA irradiationin addition to the hydrolysis of the N—Cl bond partially breaks thepolymeric chains of the nanoparticles.

Example 4 Chlorination Cycle

Chlorination/De-Chlorination Cycles of the P(MAA-MBAA) Nanoparticles:

Five chlorination/de-chlorination cycles were performed on theP(MAA-MBAA) nanoparticles. In exemplary procedures, 60 mL of theP(MAA-MBAA) nanoparticle aqueous dispersion (15 mg/mL) were chlorinatedwith 60 mL of sodium hypochlorite aqueous solution (4% w/v), followed bythe removal of excess hypochlorite as described hereinbelow. Two 1 mLsamples were removed for analysis of the bound Cl content of theP(MAA-MBAA)-Cl nanoparticles via iodometric/thiosulfate titration. Theremaining P(MAA-MBAA)-Cl dispersed in water were de-chlorinated byshaking this dispersion for 5 min with 30 mL of 0.1 N sodium thiosulfatesolution. Excess reagents were removed from the nanoparticle aqueousdispersion by extensive dialysis against water. Next, the P(MAA-MBAA)-Clnanoparticle aqueous dispersion was concentrated by water evaporation tothe original volume (60 mL). This chlorination/de-chlorination processwas repeated another four times.

The renewability of the P(MAA-MBAA)-Cl nanoparticles was evaluated forfive cycles. Table 1 below illustrates that the bound Cl content of thenanoparticles at each cycle was similar to that in the first cycle afterthe chlorination step was completed. This result proves the effectiverechargeability of these cross-linked N-halamine nanoparticles.

TABLE 1 Cycle number Bound Cl (μM/mg) 1 2.76 2 2.81 3 2.54 4 2.61 5 2.65

Example 5 Characterization Analysis

NMR:

Solid state-NMR was conducted as a complementary analysis to thecharacterization to monitor the polymerization process and distinguishbetween the chlorinated and non-chlorinated P(MAA-MBAA) NPs.

Exemplary solid state NMR experiments were performed on a Bruker AdvanceIII 500 MHz narrow-bore spectrometer, using a 4 mm double-resonancemagic angle spinning (MAS) probe. 13 C CPMAS experiments were carriedout at a spinning rate of 8 kHz, using a 2.8 us 1H 90° pulse, 2 k datapoints and a 2 ms ramped-CP period. Proton decoupling using the SPINALcomposite pulse sequence at a field of 100 kHz was used duringacquisition with a 3 s recycle delay between acquisitions. Chemicalshifts were given with respect to adamantane (38.55, 29.497 ppm).

XRD:

Powder X-ray diffraction (XRD) patterns were recorded using an X-raydiffractometer (Model D8 Advance, Bruker AXS) with Cu Ka radiation.

Zeta Potential:

Zeta potential measurements were performed by Wallis zeta potentialanalyzer (Cordouan, France).

Cryo-TEM:

The size of the dried particles was evaluated and imaged with acryogenic transmission electron microscope (cryo-TEM). Samples forcryo-TEM were prepared by placing a droplet of the solution on a TEMgrid coated with holey carbon film (lacey carbon, 300 mesh, Ted Pella,Inc.), followed by automatic blotting of the excess liquid. The specimenwas vitrified by rapid plunging into liquid ethane precooled with liquidnitrogen in a controlled environment vitrification system (Leica EM GP).The vitrified samples were transferred to a cryospecimen holder (Gatanmodel 626) and examined at −178° C. in low-dose mode. Imaging wascarried out using FEI Tecnai 12 G² equipped with Gatan 794 CCD cameraand operated at 120 kV.

Results

NMR:

The dried P(MAA-MBAA) NPs were obtained by lyophilization and wereverified by the solid-state NMR. The NMR results are summarized asfollows:

MAA monomer: ¹H NMR (solid) δ 1.93 (s, 3H, Me), 5.12 (s, 1H, vinyl),5.91 (s, 1H, vinyl), 8.38 (bs, 2H, NH₂).

¹³C NMR (solid) δ 19.80 (Me), 122.95 (CH₂-vinyl), 138.82 (C-vinyl),171.63 (C═O). P(MAA-MBAA) NPs: ¹H NMR (solid) δ 1.83 (brs, 12H, CH₂CHCH₃of MMA and 2×CH₂CH—C of MBBA), 4.77 (s, 2H, N—CH₂—N), 8.12 (bs, 4H, NH₂and NHCH₂NH)

¹³C NMR (solid) δ 18.73 (C—CH₂—C), 21.15 (Me and CH₂—CH₂—C═O), 41.87(Me-C—C═O), 45.72 (NH—CH₂—NH), 180.21 (C═O).

The P(MAA-MBAA) NPs were verified by the disappearance of the vinylicproton peaks at 5.12 and 5.91 ppm, and appearance of broad peaks of thepolymer aliphatic protons at 1-3.5 ppm. Additionally, new cross-linkermethylen protons appeared at 4.77 ppm. The chlorination was alsoverified by 1H NMR. The amide proton peak at 7-9 ppm disappeared when Hreplaced Cl, and the methylen proton peak was shifted to 5.5 ppm becauseof the chlorination of the methylen substitutions.

XRD:

XRD characterization presented in FIG. 15 demonstrate the X-raydiffraction (XRD) patterns of the MAA and MBAA monomers versus theP(MAA-MBAA) NPs and the chlorinated ones. The XRD measurements on theMAA and MBAA monomers powders display clear sharp and narrow diffractionpeaks, typically observed for crystalline materials (FIGS. 15A-B), whilethe X-ray powder diffraction of the NPs revealed very poor diffractionpatterns, pointing to the amorphous nature of the NPs (FIG. 15C-D).

Zeta Potential:

The zeta potential was also evaluated for the NPs as it may affect theirstability. The zeta potential was found to be negative; −11.3 mV and−12.72 mV for the chlorinated NPs and their non-chlorinatedcounterparts, respectively.

Cryo-TEM:

The P(MAA-MBAA)-Cl NPs were also imaged using cryo-TEM as this revealstheir dry size (FIG. 16) which was estimated to be between 5 to 9 nm.

The percent conversion (polymerization yield) of the monomers toP(MAA-MBAA) nanoparticles was calculated using the following expression:

${{Polymerization}\mspace{14mu}{yield}\mspace{14mu}\left( {{weight}\mspace{14mu}\%} \right)} = {\frac{W_{P{({{MAA} - {MBAA}})}}}{W_{({{MAA} + {MBAA}})}} \times 100}$where W_(P(MMA-MBAA)) is the weight of the obtained dried P(MAA-MBAA)nanoparticles and W_((MAA-MBAA)) is the initial weight of the monomersMA and MBAA. P(MAA-MBAA) nanoparticles of different sizes were formed byvarying various polymerization parameters, e.g., monomer concentration,initiator type, and concentration.

Example 6 Antibacterial Examination Methods

Bacterial Cultures and Growth Conditions:

In exemplary procedures, Escherichia coli (E. coli) C600, Staphylococcusaureus (S. aureus) FRF1169, and multi-drug resistant strains E. coli5327752, Klebsiella pneumoniae 5363271, and Providencia stuartii 5327311were grown overnight at 37° C. under agitation (250 rpm) in LuriaBertani (LB, Difco) growth medium.

Antimicrobial Activity Assay of the P(MAA-MBAA)-Cl Nanoparticles andNaOCl:

In exemplary procedures, the antimicrobial activity of theP(MAA-MBAA)-Cl nanoparticles was evaluated by determining the minimuminhibitory concentration (MIC) values for both E. coli and S. aureus.The MIC was defined as the lowest Cl concentration bound to thenanoparticles, or the NaOCl, at which no bacterial growth was visiblefollowing incubation with the respective bacteria. The stock solution ofthe P(MAA-MBAA)-Cl nanoparticles and NaOCl were each diluted in two-foldserial dilutions in a 96-well plate (Griener Bio-one) ranging from boundCl concentrations of 10 to 0.08 mM (approximately corresponding to 0.8%P(MAA-MBAA)-Cl, w/v) in LB medium in a 96-well plate (Greiner Bio-one).Each well contained 10⁵ colony-forming units (CFU)/mL of either E. colior S. aureus, and bacteria were either treated with P(MAA-MBAA)nanoparticles or left untreated to serve as negative controls. Thebacterial growth was monitored via absorbance measurements at OD₅₉₅utilizing a microplate reader (Synergy 2, BioTek instruments). Allexperiments were conducted in triplicate.

Bacterial-Killing Kinetics in the Presence of the P(MAA-MBAA)-ClNanoparticles and NaOCl:

In exemplary procedures, overnight cultures of E. coli and S. aureusbacteria were each diluted in a fresh LB medium to obtain stocksolutions with a working concentration of 10⁵ CFU per mL. Next, E. coliand S. aureus bacteria were grown, each with different doses ofovernight at 37° C. under agitation (250 rpm) with equivalent volumes ofeither NaOCl, P(MAA-MBAA) or P(MAA-MBAA)-Cl nanoparticles (0.2%, 0.75%,and 1% w/v) under continuous agitation (250 rpm). At various timepoints, 100 μL samples were taken from each tube and transferred intothe wells of the first row in a 96-well plate that contained 20 μL of0.1 N sodium thiosulfate. The latter was added to quench the remainingCl on the P(MAA-MBAA)-Cl nanoparticles, thus halting the reaction.Serial dilutions were carried out, and the cells were spotted onto LBagar plates, followed by incubation at 37° C. for 20 hours. Cell growthwas monitored and determined by viable cell count and expressed asCFU/mL.

Incubation of P(MAA-MBAA)-Cl NPs and NaOCl with Consecutive BacterialLoading Cycles:

The cell density of E. coli and S. aureus grown overnight was normalizedto 2*10⁵ cells per milliliter in a twofold concentrated LB medium; thenthe bacteria were treated for 1 h at 37° C. under agitation (250 rpm)with equivalent volumes of either NaOCl or P(MAA-MBAA)-Cl NPs. Bacteriashaken with water served as a negative control. After 1 h of incubation,aliquots were collected and diluted serially tenfold before spottingonto LB agar plates. After an overnight incubation at 37° C. the colonyforming units (CFU) were counted and used to determine cell survival.Immediately after each aliquot was removed, newly prepared bacteria wereadded for another hour to each of the tubes to achieve a finalconcentration of 10⁵ CFU/ml.

Antimicrobial Activity of the P(MAA-MBAA)-Cl Nanoparticles AgainstMulti-Drug Resistant (MDR) Bacteria:

In exemplary procedures, the antibacterial activity of theP(MAA-MBAA)-Cl nanoparticles was tested against three clinical isolates(blood isolates) isolated and characterized in the Tel-Aviv medicalcenter “Ichilov”: E. coli 5327752 (resistant to Gentamicin andAmpicillin), Klebsiella pneumoniae 5363271 (resistant to Gentamicin,Ciprofloxacin, and Ampicillin) and Providencia stuartii 5327311(resistant to Gentamicin, Ampicillin, and Colistin). All three strainswere grown overnight followed by dilution in LB medium to obtain aconcentration of 10⁵ CFU/mL. The bacterial suspensions were incubatedovernight with equivalent volumes of either 1.4% (w/v) P(MAA-MBAA) orP(MAA-MBAA)-Cl or 0.6% (w/v) nanoparticles. Bacteria treated withsterilized water served as an additional negative control. On thefollowing day, 10-fold serial dilutions were carried out, and thebacterial cells were plated on LB agar plates. The plates were incubatedovernight at 37° C. followed by CFU/mL determination.

Biosensor Bacteria Screening Assay:

A panel of seven modified E. coli strains (agur-Kroll, S.; Belkin, S.Anal. Bioanal. Chem. 2011, 400, 1071) was utilized for this study. Eachstrain contains a multi-copy plasmid in which the promoter of interestis fused to the Vibrio fischeri luxCDABE genes, such that promoteractivation, for example by toxic stress, drives the synthesis ofluciferase, ultimately resulting in bioluminescence. All strains werehandled alike. Bacteria were grown overnight at 37° C. under agitation(250 rpm) in LB that was supplemented with 100 mg/ml ampicillin toguarantee plasmid maintenance. The following day, the culture wasdiluted 1:100 with fresh LB media and incubated at 30° C. underagitation (200 rpm) until an OD₅₉₅ of 0.1-0.2 was reached. 100 μl ofeither distilled water or P(MAA-MBAA)-Cl NPs or their non-chlorinatedcounterparts was added in triplicate to the first row of an opaque white96-well plate (Griener Bio-one). Then all wells were filled with 100 μlof the culture, now in logarithmic phase, and 2-fold serial dilutionconducted to generate oxidative chlorine concentrations ranging from0.01 M to 0.08 mM. The plate was placed in a luminometer (in the dark)and luminescence was measured at 10′ intervals at a constant temperature(25° C.).

Bacterial killing kinetics in the presence of P(MAA-MBAA)-Cl NPs andNaOCl:

Cultures of E. coli and S. aureus bacteria grown overnight were dilutedin fresh twofold concentrated LB medium to obtain stock solutions with afinal working concentration of 10∧5 CFU/ml. Then, E. coli and S. aureusbacteria were grown with either P(MAA-MBAA)-Cl NPs or NaOCl undercontinuous agitation (250 rpm). Bacteria grown with distilled water orP(MAA-MBAA) NPs served as negative controls. At various time points, 100μl samples were taken from each tube and transferred into the first rowwells of a 96-well plate containing 20 μl of 0.1 N thiosulfate. Thelatter was added to quench the remaining chlorine on the P(MAA-MBAA)-ClNPs and NaOCl, thus terminating the sterilization process. Serialdilutions were carried out and the cells spotted onto LB agar plates,which were incubated at 37° C. for 20 h. Cell growth was monitored anddetermined by a viable cell count.

Bacterial Killing Kinetics of P(MAA-MBAA)-Cl NPs in the Presence ofAntioxidants:

Cultures of E. coli and S. aureus bacteria grown overnight were dilutedin fresh twofold concentrated LB medium to obtain stock solutions with afinal working concentration of 10⁵ CFU/ml. Then, E. coli and S. aureusbacteria were grown with P(MAA-MBAA)-Cl NPs, that were eitherpre-incubated with the antioxidants (i.e. 10% DMSO, 10 mM NAC, 10 mM AA)or water for 1 h, under continuous agitation (250 rpm). Bacteriasupplemented with distilled water or the various antioxidants served asnegative controls. At various time points, 100 μl samples were takenfrom each tube and transferred into the first row wells of a 96-wellplate containing 20 μl of 0.1 N thiosulfate. The latter was added toquench the remaining chlorine on the P(MAA-MBAA)-Cl NPs and NaOCl, thusterminating the sterilization process. Serial dilutions were carried outand the cells spotted onto LB agar plates, which were incubated at 37°C. for 20 h. Cell growth was monitored and determined by a viable cellcount.

Transmission Electron Microscopy (TEM) of Bacterial Samples:

Samples of S. aureus and E. coli cultures (10⁹ CFU/ml) or the humanosteosarcoma cell line Saos-2 ATCC HTB-85 were centrifuged immediatelyafter treatment with either distilled water, P(MAA-MBAA) NPs orP(MAA-MBAA)-Cl for the indicated time points. When indicated, S. aureusbacteria were boiled for 10′ or pre-incubated at 4° C. for 2 h beforeadding the NPs. When indicated, DMSO was incubated with the chlorinatedNPs for 1 h prior the addition of bacteria. In all the experiments, thebacteria were suspended in LB medium unless indicated otherwise. Thesamples were then fixed in 2.5% glutaraldehyde/paraformaldehyde incacodylate buffer (Electron Microscopy Sciences). The samples werewashed with cacodilate buffer and fixed in 1% osmium tetraoxide.Embedding of samples was carried out according to standard protocols (S.Croft. Electron Microscopy Methods and Protocols. In Methods inmolecular biology; 1999; pp. 117) and 60 nm thick slices were cut with adiamond knife (LBR ultratome III). The slices were deposited on bare 200mesh copper grids, and stained with 2 wt % uranyl acetate for 5 min.Finally, the grids were dried in a desiccator and examined using JEOL1200Ex transmission electron microscope at 80 kV. The percentage ofcells marked with the particles was calculated by taking 20representative microscope images containing all together 300 cells.

The Human Osteosarcoma Cell Line:

Saos-2 (ATCC #HTB-85) was maintained in Dulbecco's Minimum EssentialMedium (DMEM) supplemented with heat-inactivated fetal bovine serum 10%,penicillin 100 IU/mL, streptomycin 100 3 g/mL, and 1-glutamine 2 mM, allthese reagents were purchased from Biological Industries (Bet Haemek,Israel).

Scanning Electron Microscopy (SEM):

Samples of 10∧9 CFU/ml S. aureus cultures treated for 1.5 h with theP(MAA-MBAA) NPs or the chlorinated ones were fixed with glutaraldehydeand paraformaldehyde for 1 h. Following this incubation the samples werewashed three times with a phosphate buffer saline (PBS). Samples werethen immersed for 1 h in titanic acid and a glutamate solution in a 4:5ratio concentration, respectively. Samples were afterwards washed threetimes with PBS and exposed to an osmium tetraoxide solution for 1 h. Todehydrate the samples, they were sequentially washed with water-ethanoland ethanol-Freon solutions (concentrations ranging from 50% to 100% foreach solvent). Finally, the samples were dried in air for at least 24 hand then coated with a layer of carbon and examined using a FEI Quanta200 FEG enviromental scanning electron microscope.

Results Antimicrobial Activity Assay of the P(MAA-MBAA)-Cl Nanoparticlesand NaOCl

The characterizing the bactericidal potential of P(MAA-MBAA)-Cl NPs wasevaluated relative to the soluble non-nanometric N-halamine polymerMAA-Cl (i.e. PMAA-Cl) and to NaOCl, the chemical that was used to loadthe P(MAA-MBAA)-NPs with oxidative Cl and is the active ingredient ofhousehold bleach, one of the most commonly used disinfectants in theworld. All three reagents release Cl⁺ that kills bacteria and theoxidative chlorine concentrations used were 11 mM and 8 mM. As presentedin Table 2 hereinbelow, the chlorinated NPs and NaOCl killed both E.coli and S. aureus, while the PMAA-Cl was much less effective and killedonly S. aureus. These results show that P(MAA-MBAA)-Cl NPs and NaOCl aremore effective than the non-nanometric PMAA-Cl.

TABLE 2 Reagent name E. coli S. aureus P(MAA-MBAA)-Cl NPs (11 mM) Totalkill Total kill P(MAA-MBAA)-Cl NPs (8 mM) Total kill Total kill PMAA-Cl(11 mM) 6 logs (out of 10) Total kill PMAA-Cl (8 mM) No killing Totalkill NaOCl (11 mM) Total kill Total kill NaOCl (8 mM) Total kill Totalkill

Next, the minimum inhibitory concentration (MIC) of the two agents wasdetermined. E. coli and S. aureus were exposed to serial dilutions ofeither P(MAA-MBAA)-Cl NPs (aqueous dispersion) or NaOCl. The MIC of thetwo reagents was found to be the same, 5.6 mM oxidative Cl, for both E.coli and S. aureus. Notably, bacteria exposed to non-chlorinatedP(MAA-MBAA) NPs did not exhibit growth arrest and behaved like untreatedbacteria.

Incubation of P(MAA-MBAA)-Cl NPs and NaOCl with Consecutive BacterialLoading Cycles:

The capability of chlorinated NPs versus NaOCl to withstand repetitivecycles of bacterial exposure. To this end, both E. coli and S. aureuswere incubated with either NaOCl or the chlorinated NPs. Thisconcentration was applied in all the experiments, unless indicatedotherwise. Every hour a sample was taken from each tube and plated onagar plates, and in parallel 10⁵ CFU/ml freshly prepared bacteria wereadded. In total, 8 bacterial loading cycles were conducted. As presentedin FIG. 17, the P(MAA-MBAA)-Cl NPs retained activity throughout theexperiment, eradicating both E. coli and S. aureus. In contrast, NaOClwas no longer able to promote bacterial killing from cycle 4 for E. coliand from cycle 2 for S. aureus. It is to note that the quantity ofbacteria exposed to bleach throughout the loading cycles did not reachthe concentration of bacteria residing in the control test tube (i.e.,untreated bacteria) (FIG. 17), suggesting that the bactericidal activityof bleach during this short incubation has been hampered. To investigatethis premise, we checked the viability of bacteria sampled following anovernight incubation. After a longer exposure time to NaOCl, there wereno viable E. coli bacteria which suggests that given enough time bleachstill managed to kill the bacteria, whereas the S. aureus bacteria wereable to overcome the growth inhibitory affect observed following theshort exposure. These data demonstrate that S. aureus bacteria are moreresistant to bleach than E. coli. Importantly, after an overnightincubation with P(MAA-MBAA)-Cl NPs, neither E. coli nor S. aureusbacteria were viable (FIG. 17).

Antibacterial Properties of the P(MAA-MBAA)-Cl Nanoparticles:

The killing kinetics following incubation of either E. coli or S. aureuswith increasing concentrations of the P(MAA-MBAA)-Cl nanoparticles,namely, 0.2%, 0.75%, and 1% (w/v), was monitored. Samples were collectedat various time points of: 0, 2, 5, 15, 30, and 60 min. Although 0.2%P(MAA-MBAA)-Cl nanoparticles partially attenuated the growth of E. coliby 15′ and complete elimination was obtained at 30′ (FIG. 18A), fulleradication was achieved for S. aureus at 30′, and no effect wasobserved at 15′ (FIG. 18B), suggesting that the P(MAA-MBAA)-Clnanoparticles act more slowly on S. aureus than on E. coli. At aconcentration of 0.75% P(MAA-MBAA)-Cl nanoparticles, both types ofbacteria were completely killed at 15′, demonstrating dose-dependentkinetics. Furthermore, at 1% P(MAA-MBAA)-Cl nanoparticles, no viable E.coli bacteria were detected after 2′ (FIG. 18A) and no viable S. aureusafter 5′ (FIG. 18B), further demonstrating that E. coli have a highersusceptibility to the P(MAA-MBAA)-Cl nanoparticles than do S. aureus. Inaddition, non-chlorinated P(MAA-MBAA) nanoparticles was used at the sameconcentrations used for P(MAA-MBAA)-Cl nanoparticles as a negativecontrol, but because these nanoparticles did not affect the bacterialgrowth at all applied concentrations, only the results for the highestconcentration used, i.e., 1% P(MAA-MBAA) nanoparticles is presented.

Antibacterial Activity of the P(MAA-MBAA)-Cl Nanoparticles Against MDRBacteria:

antibacterial activity of the P(MAA-MBAA)-Cl nanoparticles against MDRbacteria was tested, as described hereinabove. The bacterial strainschosen for this analysis were clinical isolates of E. coli 5327752(resistant to Gentamicin and Ampicillin), Klebsiella pneumoniae 5363271(resistant to Gentamicin, Ciprofloxacin, and Ampicillin), andProvidencia stuartii 5327311 (resistant to Gentamicin, Ampicillin, andColistin). These bacteria are highly resistant to many of theantibiotics available to date and thus pose a serious public healththreat because they are more difficult to eradicate. As presented inFIG. 19, all three bacteria strains were completely killed followingincubation with the P(MAA-MBAA)-Cl nanoparticles as opposed to thosegrown in the presence of the non-chlorinated nanoparticles or sterilizedwater. Taken together, these results suggest that P(MAA-MBAA)-Clnanoparticles offer the potential to treat multidrug-resistant bacteria.

Bacterial Killing Kinetics in the Presence of P(MAA-MBAA)-Cl NPs andNaOCl:

The killing kinetics of P(MAA-MBAA)-Cl NPs and NaOCl reagents in thepresence of E. coli (FIG. 20A) or S. aureus (FIG. 20B) were compared. Inline with the observed differences in the oxidative chlorine releasekinetics, NaOCl acted faster, eradicating both types of bacteria within2 minutes of exposure, in comparison to the chlorinated NPs thateliminated the same amount of bacteria only after 30 minutes (FIG. 20).In summary, the data show that bleach exerts its antimicrobial activityfaster than the NPs, however, in the long run P(MAA-MBAA)-Cl NPs exhibitsuperior stability and efficacy, especially under adverse environmentalconditions that contain high organic load like proteinaceous materials.Therefore, P(MAA-MBAA)-Cl NPs should be the reagent of choice.

Biosensor Bacteria Screening Assay:

To understand better the mechanism whereby the P(MAA-MBAA)-Cl nanoagents exert their toxic effects, biosensor E. coli bacteria created byBelkin and colleagues were utilized, as described hereinabobe. Thegenetically-engineered bacteria harbor plasmid bioluminescence lux genesfused to specific stress response promoters, and thus can be exploitedto monitor activation of stress responses, such as heat shock, DNAdamage, oxidative stress, and fatty acid metabolism disruption. Of allthe bacteria screened, only E. coli strains harboring a plasmidcontaining either micF::luxCDABE or sodA::luxCDABE fusion weresignificantly induced by the P(MAA-MBAA)-Cl NPs in comparison tobacteria treated with either water or non-chlorinated NPs (FIG. 21). Itis important to note that this response was observed only when a lowerdose (5.5 mM) of the chlorinated NPs was applied that was not highenough to induce massive cell death, but was sufficiently high to inducethe bacterial defense pathways. sodA and micF are both responsive tooxidative stress and their induction by P(MAA-MBAA)-Cl NPs likelyreflects the mechanism underlying bacterial killing. Superoxidedismutase (i.e., sodA) catalyses the transition of superoxide (O²⁻) tooxygen and H₂O₂, and then catalase and peroxidase prevent theaccumulation of H₂O₂ within the cell by converting it to H₂O and O₂.Accordingly, SodA is considered a key enzyme in E. coli oxidative stressresponse. The micF gene encodes a non-translated antisense RNA thatbinds the mRNA of the outer membrane porin protein (OmpF), triggeringOmpF degradation and hence represents a negative regulator. OmpF formspores at the outer cell membrane, allowing the passive diffusion ofsmall hydrophilic molecules across the membrane.³⁵ Regulation of outermembrane permeability critically influences survival of the bacteria inresponse to environmental stress. Indeed, various environmental factorshave been shown to be involved in MicF-mediated reduction of OmpFlevels, such as oxidative stress, nutrients depletion and increasedosmolarity.

TEM Examination:

To investigate in more detail the mechanisms underlying theantibacterial activity of P(MAA-MBAA)-Cl NPs, transmission electronmicroscopy (TEM) was conducted to examine if the NPs exert morphologicaleffects on the bacteria. We did not observe any detectable morphologicalchanges within S. aureus bacteria following treatment with thechlorinated NPs for 1.5 h (FIG. 22), which corresponds to the timeneeded to kill 10∧9 CFU/ml of these bacteria (data not shown). However,we did observe the formation of very organized structures of particlesaround the bacteria, specifically accumulating at the cell wall andencircling it like “necklaces” (FIG. 22A). Remarkably, these particleswere not observed in the extracellular space, suggesting a specificinteraction of these particles with the bacteria. Of note, these layersof particles did not surround cells treated with distilled water (datanot shown) or non-chlorinated NPs (FIG. 22A), suggesting that theoxidative chlorine on the NPs is responsible for this unusualphenomenon. Moreover, the particles decorated the bacteria already at15′, revealing not only a specific interaction with the bacterial cells,but also a rapid one (FIG. 22B). The proportion of cells marked withthese particles was quantified and found that 100% of the cellsexhibited these structures after only 15′ (n=300), although some cellswere encircled with less particles than others.

Without being bound by any particular theory, one interpretation of thedata is that these particles are the P(MAA-MBAA)-Cl NPs themselves.Another option is that cellular material is secreted by the bacteria dueto the stress imposed by the chlorinated NPs, although the latter isless likely due to the rapid appearance of the particles on the cellsurface. To differentiate between these options, NPs 6 times larger thanthose utilized hereinthroughout were synthesized, i.e., 190±20 nm asopposed to 27±3 nm hydrodynamic diameter according to dynamic lightscattering (DLS) measurements (FIG. 23A). As described hereinabove, thecryo-TEM images presented in FIGS. 16 and 23B illustrate the differencein dry size; the small NPs are about 3-15 nm while the large NPs aremostly aggregates of 100-200 nm. As presented in FIG. 23C, bacteriatreated with the larger NPs were indeed surrounded by larger particles,the size of which matched the TEM measurements of NPs alone (FIG. 23B).Notably, although the larger P(MAA-MBAA)-Cl NPs associated mainly withthe bacterial cells, there were some aggregates in the extracellularenvironment unlike the observations of the small NPs, which were onlyobserved surrounding the bacteria. This finding suggests that the smallNPs may be more target specific and therefore, superior for bacterialkilling. These data support the model that the chlorinated NPsspecifically interact with the bacteria via oxidative chlorine releaseand inflict toxic effects on the bacteria that are trapped within thesenanocages. These nanocaging was further illustrated via SEM images thatshow the NPs' 3D morphology (FIG. 24). These data suggest thatchlorinated NPs have a uniquely strong tendency to adhere and circle thebacterial cell wall rather than aggregate. Moreover, the observationthat every bacterium was marked with chlorinated NPs, further emphasizestheir potency as an anti-bacterial agent. Of note, no pronouncedappearance of NPs around E. coli was detected (FIG. 25), which could beexplained by the different cell wall composition of Gram-negative versusGram-positive bacteria.

To determine if the gathering of the chlorinated NPs at the cell wall ofS. aureus requires energy, the cells were either pre-incubated at 4° C.for 2 h or thermally killed (i.e. boiled for 10 minutes) before addingthe NPs. As shown in FIG. 26, inactivating the metabolic state of S.aureus or killing it did not abrogate the formation of the structuresaround the cells, suggesting neither energy nor cellularproteins/enzymes are required for this interaction to occur. Moreover,using the antioxidant DMSO did not abolish the bacterial decoration bythe P(MAA-MBAA)-Cl NPs, suggesting ROS formation is not a prerequisitefor this tagging either (FIG. 26). Nevertheless, when the NPs were mixedwith bacteria suspended in water, the cells were barley marked with theparticles (FIG. 27), which may imply that some component/s found in LBis mediating the interaction between the bacteria and the NPs. Ofimportance, the zeta potential of the NPs becomes positive when LB isadded to the particles' suspension, i.e. 1.59 mV (as opposed to thenegative value received from the suspension itself). This may suggestthat the attraction of the NPs to the bacteria is favored when LB isadded due to the positively charged NPs that are now attracted to thenegatively charged bacterial surface.

Targeting Mammalian Cells:

In additional exemplary procedures, the ability of the charged NPs totarget mammalian cells was examined, using the osteosarcoma cell lineSaos-2. As can be seen in FIG. 28, no particles were observed around theSaos-2 cells, whether the P(MAA-MBAA) or the P(MAA-MBAA)-Cl NPs wereapplied. It is concluded that S. aureus bacteria are specifically markedfor destruction by the chlorinated NPs, which unload their oxidative Clcargo and eliminate the bacteria.

Since there were no noticeable morphological changes followingincubation with P(MAA-MBAA)-Cl NPs for 1.5 h, the incubation wasextended to 5 h and 15 h. After 5 h and 15 h of incubation with thechlorinated nanosized agents, membrane ‘snail-like’ structures wereobserved to accumulate within the S. aureus cells, (FIG. 29). Thisphenomenon was not detected within cells treated with non-chlorinatedNPs (FIG. 29) or distilled water (data not shown), suggesting that theoxidative chlorine provoked directly or indirectly the formation ofthese tightly packed intracellular membrane structures.

Example 7 Examination of P(MAA-MBAA)-Cl NPs in Organic Media Methods

Determining the Stability of the P(MAA-MBAA)-Cl NPs and NaOCl in OrganicRich Media:

1 ml of either DDW, NaOCl or P(MAA-MBAA)-Cl NPs was mixed with 1 ml oftwofold concentrated LB medium and incubated for 3 h, 5 h or 24 h. Then,E. coli or S. aureus were added to each of the solutions, reaching afinal concentration of 10∧5 CFU/ml and the mixture agitated for either 3h or 24 h. At the indicated time points, samples were taken for cellviability determination and the solutions were reloaded with freshlyprepared bacteria. The experiment was continued until the reagents wereno longer capable of evincing toxic effects on the tested bacteria.

Kinetics of Oxidative Chlorine Release from the Charged NPs and NaOCl inthe Presence of Organic Rich Media:

Equal volumes of NaOCl or P(MAA-MBAA)-Cl NPs were incubated withequivalent volumes of twofold concentrated LB medium. The preciseconcentration of the oxidative chlorine found on the two reagents wasdetermined at different time intervals via quenching with sodium iodidefollowed by spectrophotometer (Amersham Bioschiences) measurements atwavelengths of 292 nm and 350 nm, as previously described.

Kinetics of Oxidative Chlorine Release from the Charged NPs and NaOCl inthe Presence of Organic Rich Media:

Equal volumes of NaOCl or P(MAA-MBAA)-Cl NPs were incubated withequivalent volumes of twofold concentrated LB medium. The preciseconcentration of the oxidative chlorine found on the two reagents wasdetermined at different time intervals via quenching with sodium iodidefollowed by spectrophotometer (Amersham Bioschiences) measurements atwavelengths of 292 nm and 350 nm.

ESR Measurements:

ROS production was detected using the ESR spin trapping techniquecoupled with a spin trap 5,5-Dimethyl-pyrroline N-oxide (DMPO, Sigma,St. Louis, Mo.). Typically, the aqueous suspensions of NPs were added toDMPO (0.01 M), in the presence of equivalent volumes of either twofoldconcentrated LB medium, or each of its components (Tryptone, yeastextract, NaCl) or water. Whenever indicated the following antioxidantswere added to the reaction: 10% DMSO, 10 mM N-acetyl cycteine (NAC) and10 mM Ascorbic acid (AA), all were purchased from Sigma. The solutionwas drawn into a 0.8 mm ID capillary quartz tube sealed at both endswith a plastic Critoseal (Thermo Fisher Scientific Inc), which wasplaced into a quartz tube that in turn was placed into the EPRrectangular cavity (ER 4122SHQ). The measurements were taken using aX-band Elexsys E500 EPR spectrometer (Bruker, Karlsruhe, Germany) usingthe following parameters: microwave power, 20 mW; scan width, 100 G;resolution, 1024; Gain, 60; sweep time, 60 s; # scans, 2; modulationfrequency, 100 kHz; modulation amplitude, 1 G. In order to compare theradical intensity, the double integration (DI) of the spin adduct signalwas calculated, using the Xepr 2.6b.58 acquisition version.

Results

The stability of chlorinated NPs versus bleach in full organic media(i.e. LB) was compared. As described hereinabove, under “Methods”,P(MAA-MBAA)-Cl NPs and NaOCl were pre-incubated with LB for differentperiods: 3 h, 5 h or 24 h. After this initial incubation with organicmedia, E. coli or S. aureus bacteria were supplemented to a finalconcentration of 10∧5 CFU/ml, and samples were taken after a further 3 hor 24 h of incubation. As shown in FIG. 30A, pre-incubation of NaOCl orchlorinated NPs with LB for 3 h prior to addition of E. coli had noimpact on their bactericidal activity. However, pre-incubation of NaOClwith media for 3 h prior to addition of S. aureus did compromise itsbactericidal activity, as the reagent was subsequently only capable ofevincing complete killing by 24 hours (FIG. 30B). In contrast,pre-incubation of P(MAA-MBAA)-Cl NPs with media for 3 h prior toaddition of S. aureus had no impact on its bactericidal activity, withcomplete killing observed after 3 h (FIG. 30B). Pre-incubation of NaOClwith media for 5 h prior to addition of E. coli resulted in growthinhibition at the 3 h time point, with bacteria viability reduced byalmost 4 logs; complete killing was evident only at 24 h (FIG. 30C). Thesame conditions elicited growth arrest for S. aureus (FIG. 30D), furthercorroborating our premise that E. coli are more sensitive to bleach thanS. aureus. Remarkably, pre-incubation of P(MAA-MBAA)-Cl NPs with LB for5 h prior to addition of E. coli or S. aureus did not compromise itsbactericidal activity (FIGS. 30C-D). Finally, pre-incubation of NaOClwith LB for 24 h prior to addition of E. coli or S. aureus destroyed itsantibacterial activity, such that the bacteria grew comparably tountreated controls (FIGS. 30E-F). In sharp contrast, pre-incubation ofP(MAA-MBAA)-Cl with LB for 24 h prior to addition of E. coli or S.aureus did not compromise its bactericidal activity (FIG. 30E-F). Insummary, P(MAA-MBAA)-Cl NPs exhibit superior stability to organicmaterials as compared to bleach.

Having established that chlorinated NPs are still toxic towards bacteriadespite pre-exposure to organic rich media for 24 h, the longer-termactivity of P(MAA-MBAA)-ClNPs was examined. To this end, P(MAA-MBAA)-ClNPs were exposed to repetitive bacterial loading cycles for up to 17days. The chlorinated NPs retained bactericidal activity over 6 loadingcycles of E. coli spread over 9 days, but by the seventh cycle (on thetenth day) bacterial growth was only partially attenuated, and by theninth loading cycle (day 12) the E. coli grew comparably to untreatedcontrols (FIG. 31A). As for S. aureus, the chlorinated NPs continuedkilling the bacteria for nine consecutive cycles spread over 12 days,with bacterial growth only detectable on the following cycle (FIG. 31B).Taken together, the data demonstrate that nanosized P(MAA-MBAA)-Cl aremore stable than NaOCl when exposed to organic materials. It was ofinterest to check at which concentration NaOCl retained the capabilityto kill bacteria, when the NaOCl was pre-incubated for 1 week with LBmedia. To address this, we took a sample of fresh NaOCl straight from acommercial bottle, corresponding to 0.72 M, incubated it with LB mediumfor 1 week and then added bacteria. Interestingly, it was found that0.36 M of NaOCl, which is 33 times more than the concentration of theoxidative Cl bound to the NPs, is required to kill E. coli and S.aureus, with 0.18 M NaOCl ineffective (FIG. 32). This findingunderscores the advantages of using chlorinated NPs over NaOCl, both interms of stability and efficacy.

To investigate in more detail the stability of P(MAA-MBAA)-Cl NPs, theoxidative chlorine content of the chlorinated NPs versus bleach afterincubation in LB medium for 11 days was measured. The oxidative chlorineconcentration was determined using a spectrophotometer at 292 nm (FIG.33A) and 350 nm (Figure FIG. 33B). A surge in NaOCl consumption uponexposure to LB was observed, as the oxidative Cl release from NaOCl wasvery rapid, with almost 50% of the NaOCl molecules sequestered byorganic substances after only 10 minutes of incubation in the medium(FIG. 33). In contrast, approximately 90% of the NPs retained theirchlorinated form, suggesting a gradual decay of the Cl⁺ from the NPs asopposed to the rapid decay observed for NaOCl. Still, this amount ofreleased Cl⁺ was sufficient to induce bacterial killing even followingseparation of the loaded NPs as presented in FIG. 34. Furthermore, after1 day of incubation we could barely detect Cl⁺ on NaOCl, with 0.9% and0.5% chlorinated according to measurements at 292 nm and 350 nm,respectively (FIG. 33), whereas 12% of NPs retained Cl⁺. Taken together,the data indicate that the organic materials in the medium scavenge theCl⁺ in NaOCl, compromising its activity and rendering bleach unable tokill bacteria. However, chlorinated NPs are far more stable, resist thescavenging nature of the organic material and hence, exhibit extendedantibacterial activity under these conditions.

ESR Measurements:

In view of the oxidative activation of the two reporter strains asdescribed hereinabove, ESR measurements were carried out to determinedirectly whether the chlorinated NPs generate Reactive Oxygen Species(ROS), using 5,5-dimethyl-1-pyrroline-N-oxide (DMPO) to trapoxygen-centered free radicals. The DMPO spin trap reacts with ROS, suchas, hydroxyl radicals or superoxide anion radicals, to produce the spinadducts DMPO-OH or DMPOOH, respectively. The DMPO-OH is a relativelystable paramagnetic species with a characteristic EPR signal of 1:2:2:1quartet. It was observed a typical ESR spectrum of DMPO-OH, giving riseto four resolved picks (FIG. 35), suggesting the formation of hydroxylradicals (.OH). Of note, these radicals were formed only followingexposure of the nano-sized P(MAA-MBAA)-Cl to organic reagents like LBmedia, and not when the chlorinated NPs were suspended in water (FIG.35), revealing a target-specific mode of action. To further elucidatewith what components in the LB medium the chlorinated NPs interact withto generate the hydroxyl radicals, each of the materials found withinthis growth medium (i.e. Tryptone, yeast extract and NaCl) was exposedto the P(MAA-MBAA)-Cl NPs. Only the Tryptone and the yeast extracttriggered ROS formation by the NPs as opposed to NaCl which did notinteract with the particles (FIG. 36), emphasizing the specificity ofthe charged NPs towards organic materials. This remarkable specificityis not exhibited by NaOCl. Without being bound by any particular theory,it is assumed that the ROS are generated directly or indirectly by theoxidative chlorine attached to the NPs, since non-chlorinated NPs didnot provoke the formation of hydroxyl radicals (FIG. 35). It isimportant to note that the charged NPs are capable of killing bacteriasuspended in water (FIG. 37), as the chlorinated NPs can exert toxicityvia a direct transfer of the oxidative chlorine to a bacterialassociated component.

.OH free radicals are extremely toxic and notorious for their ability tocause cellular damages, including DNA damage and oxidation of lipids andamino acids in proteins. Thus, without being bound by any particulartheory, the formation of ROS by P(MAA-MBAA)-Cl provides a mechanisticbasis whereby these NPs exert detrimental effects. The proposedrelationship between ROS production and bacterial killing iscorroborated by our finding that lower concentrations of chlorinated NPsare associated with reduced production of the DMPO-OH quartet signal,and in turn, partial killing of bacteria (FIG. 38). In fact, lowconcentrations (1.25 mM) of P(MAA-MBAA)-Cl that do not kill the bacteria(FIG. 38) hardly trigger formation of ROS (FIG. 38). In summary, theCl⁺-charged NPs promote formation of ROS, which triggers theoxidative-type stress response and ultimately, results in cell death.

To further corroborate that the chlorinated NPs trigger formation of —OHand that these radicals are the cause for the antibacterial activityimparted by the NPs, exploited dimethyl sulfoxide (DMSO), N-acetylcysteine (NAC) and Ascorbic acid (AA) were exploited as potent hydroxylradical scavengers, serving as an established means of mitigating thedeleterious effects of .OH. In line with a model that mixingP(MAA-MBAA)-Cl NPs with organic reagents leads to ROS formation, DMSOaddition reduced the levels of DMPO-OH by 60%, while NAC and AAcompletely abrogated the formation of DMPO-OH (FIG. 39A). In light ofthese results, the effect of these antioxidants on the chlorinated NPs'antibacterial activity was examined. While the P(MAA-MBAA)-Cl NPs killedboth E. coli (FIG. 39B) and S. aureus (FIG. 39C) in the presence of LBalready after 15′, pre incubation of the chlorinated NPs with either NACor AA prior the addition of bacteria, abolished the killing propertiesof the NPs (FIGS. 39B-C). Of note, DMSO was less efficient at mitigatingbacterial cell death, as after 60′ E. coli bacteria were eliminatedwhile at 90′ the P(MAA-MBAA)-Cl NPs started to affect the growth of S.aureus (FIGS. 39 B-C), which was also reflected by the capacity of DMSOto compromise, but not eliminate the charged NPs' ability to mediatehydroxyl radicals formation (FIG. 39A).

Example 8 Degredation of Organic Materials Method

To investigate the capability of P(MAA-MBAA)-Cl nanoparticles to degradeorganic materials (i.e. self-cleaning properties), two easy-to-followorganic dyes, methylen blue (MB) and crystal violet (CV), were selected.

The P(MAA-MBAA)-Cl nanoparticle dispersion were shaken with the dyes andthe concentration was monitored by spectrophotometer up to fulldegradation of the dye. The effect of two parameters, i.e. theincubation temperature and the nanoparticles concentration, on the dyesdegradation was investigated.

In exemplary experiments, 200 μl of MB or CV (0.1 mg/ml) aqueoussolution was mixed with 1.8 ml (8 mg/ml) of P(MAA-MBAA)-Cl nanoparticlesaqueous dispersion in a 2 ml Eppendorf. Four different incubationtemperatures were tested, i.e. room temperature, 50° C., 70° C., and 90°C. The concentration of MB and CV was monitored by spectrophotometer atthe range of 500-750 nm to detect the main peaks at 666 nm and 597 nm,respectively. Samples were taken every 30 min for the first 5 h, then inlarger time intervals until total disappearance of the peak. At 50, 70,and 90° C. the peak vanishes within the first 4 h. The experiments wereperformed in triplicates. The values were normalized relative to the dyeconcentration at the beginning of the experiment.

To assess the effect of the P(MAA-MBAA)-Cl nanoparticles concentrationon the model dyes degradation, the same procedure was conducted at 90°C., using 1.8 ml of either 8 mg/ml or 1.6 mg/ml, of P(MAA-MBAA)-Clnanoparticles and the analysis was performed as mentioned above.

Results

The “self cleaning” ability of the P(MAA-MBAA)-Cl nanoparticles wasdetermined using two model organic dyes, crystal violet (CV) andmethylene blue (MB). Overall, CV was decomposed by the P(MAA-MBAA)-Clnanoparticles faster than MB, as indicated by the comparison betweenFIG. 40 and FIG. 41.

Furthermore, the temperature significantly affected the degradationrates of the dyes by the P(MAA-MBAA)-Cl nanoparticles. Kineticexperiments at room temperature indicated that complete decomposition ofCV and MB occurs after 80 and 120 h of incubation, respectively (datanot shown). After 1 h of incubation at room temperature, 15% and 60% ofthe initial concentration of CV and MB were left, respectively. At 50°C., the complete degradation time of MB and CV was drastically shortenedto 4.5 h and 3 h, respectively. The degradation rate shortened even moreat 70° C. when complete degradation was achieved by incubation with thechlorinated nanoparticles for 3 h and 1 h, respectively. The fastest dyedegradation was completed by heating the dyes solution with thechlorinated nanoparticles to 90° C. At this temperature, the totaldegradation of MB appeared within an hour of incubation and up to 30 minfor the total degradation of CV.

Example 9 Antibacterial Coatings

Coating PET Films with P(MAA-MBAA) Nanoparticles:

Coatings of P(MAA-MBAA) nanoparticles onto A4 PET(polyethyleneterpthalate) films were prepared by suspending dryP(MAA-MBAA) nanoparticles (1.16 g) in a water based solvent resinsolution (6.64 g, from Hanita Coatings Industry Ltd, Israel) for 5 h atroom temperature. The particles' dispersion was then spread on the 23 μmPET film with a Mayer Rod, following by drying the P(MAA-MBAA) coatingon the PET film for 1 minute at 120° C. and then for additional 3 h at60° C. The dry P(MAA-MBAA)/PET film was then cut to the specimens of 5cm long and 4 cm wide.

Chlorination of the PET Films Coated with the P(MAA-MBAA) Nanoparticles:

Specimens of 5 cm long and 4 cm wide of the P(MAA-MBAA)/PET films werecut. The active chlorine source, sodium hypochlorite solution (5% w/v),was adjusted to pH=7 by acetic acid titration. The P(MAA-MBAA)/PET filmspecimens were inserted to a flask containing the hypochlorite solutionand then shaken for 30 min followed extensive rinses (50 mL) with waterand dried by condensed air.

The bound-Cl content of the P(MAA-MBAA)-Cl/PET films was 3.75×10⁻⁵ molper specimen as determined by iodometric/thiosulfate titration by thefollowing expression:

${{bound}\text{-}{{Cl}({mM})}} = \frac{N \times V \times 1000}{2}$where N is the normality (equiv/L) and V is the volume (L) of thetitrated sodium thiosulfate solution.

Antibacterial Activity of P(MAA-MBAA)-Cl-Coated PET Films:

P(MAA-MBAA)-Cl-coated PET films at three different coating thicknesses(i.e. 1, 4 and 7.8 g/m2) were tested for their antibacterial propertiesusing E. coli and S. aureus, representing Gram-negative andGram-positive bacteria, respectively, as described hereinabove. 1 ml ofLB 1% containing either E. coli or S. aureus at a concentration of 10⁵CFU/ml were incubated overnight with the different films, each one at adimension of 0.5 cm×4 cm or were left untreated (i.e. control). On thefollowing day, samples of 200 μl were taken from each tube andtransferred into the wells of the first row in a 96-well plate. Serialdilutions were carried out and the cells were spotted onto LB agarplates, followed by their incubation at 37° C. for 20 h. Cell growth wasmonitored and determined by viable cell count.

Results

As shown in FIG. 42, films at coating thicknesses of 4 and 7.8 g/m²managed both to kill all the bacteria no matter which bacterial strainwas applied. Nevertheless, films at a coating thickness of 1 g/m² wereless efficient against E. coli, demonstrating a reduction of 4 logs,while S. aureus bacteria were more susceptible to the coating, and assuch were completely eradicated.

Example 10 Sewage Experiments Methods

Master Batch and PE/P(MAA-MBAA) Composite Nanoparticles ProfilePreparation:

Antimicrobial plastic profiles were produced by dry mixing of linear lowdensity polyethylene (LLDPE) with 1% of the P(MAA-MBAA) nanoparticles ina cast extrusion machine at 230° C. Samples in absence of thenanoparticles were also prepared and used as control.

Chlorination of the PE-P(MAA-MBAA):

cylinders of 8 cm length and radius of 1 cm of the PE/P(MAA-MBAA)profiles were shaken with 50 ml of sodium hypochlorite (4% w/v,neutralized by acetic acid for an hour, then washed four times withwater (ddw) and dried with condensed air.

“Shafdan” Sewage Protocol:

Four pipes (32 mm) were connected to wasterwater from the ShafdanTreatment Plant which contains the household as well as the industrialwastewater of the Dan region (about 60% of Israel population). Theflowing rate was maintained at 10 L/h. The chlorinated PE/P(MAA-MBAA),short name: PE/Cl-NPs, profiles were placed in the pipes for time rangesof month or two then were pictured immediately and recharged or placedagain without any treatment for another cycle according the detaileddescription at the results section. This charging-recharging process wasrepeated 4 times.

Protein Determination Kit:

Quantification of the organic matter found on all the various profileswas done via the Bicinchoninic Acid (BCA) protein determination kit(Pierce).

Results

“Shafdan” Sewage:

The results are demonstrated in FIGS. 43A-E, and it can be observed thatthe leftmost PE profile which rechlorinated before every cycle appearsto stay clean from bacteria and organic residues while the negativecontrol, the rightmost sample, looks dirty i.e. full of biofilm coating.The two middle profiles which made almost the same way of chlorination,appears to look almost the same.

First Cycle

(FIG. 43B): 8 cm PE/NPs and PE/Cl-NPS profiles in pipes were dipped forthe first time for a month in flowed Shafdan waste water.

Second Cycle

(FIG. 43C): additional month in the Shafdan waste water. The sampleswere divided to 4 cm length in order to enlarge the experiment options.The left-facing arrows mark samples that were chlorinated, the two othersamples were dipped with any other treatment.

Third Cycle

(FIG. 43D): additional month in the Shafdan waste water. The left sampleonly was rechlorinated.

Forth Cycle

(FIG. 43E): additional two months in the Shafdan waste water. The rightsample was the only which was not treated.

It can be observed that the leftmost profile which rechlorinated beforeevery cycle looks clean from bacteria and organic residues while thenegative control, the rightmost sample, looks dirty full of biofilms.The two middle profiles which made almost the same way of chlorination,looks almost the same.

Protein Determination Kit:

As shown in FIG. 44A, profiles that were chlorinated prior to theirincubation in Shafdan water but not in the second regeneration cycle(denoted as “I/O”) have demonstrated a reduction of 16% in the organicbiomass while profiles that were not chlorinated in the first cycle butonly in the second one showed a decay of 37% in comparison to thecontrol (denoted as “0/0”). The most prominent decay was achieved byprofile I/I, in which the nanoparticles embedded within the profile wereloaded with chlorine at both cycles (i.e. 63%). The protein analysis wasalso conducted at the end of the experiment (two months after the forthcycle was carried out). The profile that was chlorinated throughout allthe experiment (denoted as “I/I/I/I”) managed to reduce the proteinquantity by 61% (FIG. 44B), while profiles that were chlorinated in thefirst or second cycles in addition to chlorine recharging in the thirdcycle have led to similar decays of 45% and 52%, respectively (FIG.44B). It is important to emphasize that the reductions were probablymore significant if all the organic matter found on the control wasreduced in the experiments. Nevertheless, on the other profiles it couldbe seen that the NaOH lysis treatment managed to remove all the biomass.This might be due to the fact that the control profile contained suchhigh load of biomass that the lysis treatment was not sufficient enoughto remove all of the biomass and/or that the organic fouling is composednot only from proteins, but most likely from polysaccharides, lipids andnucleic acids as well, and thus other quantification methods should beapplied.

Example 11 Anti-Fouling Coating on Dripper Method

200 drippers that had been imbedded with P(MAA-MBAA) NPs being eitherchlorinated using NaOCl or left untreated (i.e. control) were incubatedin field study facility (operated by Netafim LTD.). After one month ofincubation under constant flow of sewage treated irrigation water, thedrips containing the chlorinated NPs had less biofouling as opposed tothe control which had fouling on it (FIG. 45A). These results werevisualized using environmental scanning electron microscopy (E-SEM)(FIG. 45B) and were further quantified via total organic carbon (FIG.45C).

After 2.5 months of incubation in Hazerim, the results were still verysignificant, showing a clear difference between the control drippers tothe treated ones. In addition, chlorinated drippers were taken after onemonth of incubation in Hazerim for regeneration with Cl⁺, using NaOCl.The regenerated drippers were returned to the field and stored again inHazerim for an additional month, and as shown in FIG. 46, theregenerated drips stayed cleaned and no fouling was observed on them.The experiments are still ongoing, but currently chlorinated drippersprevented fouling for more than 5 months.

Example 12 Cytotoxic Assays Method

Mouse fibroblasts BALB/c 3T3 and rat alveolar macrophages NR8383 celllines were both purchased from ATCC and cultured in petri dishes ineither Dulbecco's Modification of Eagle's Medium (DMEM, ATCC 30-2002)containing 4 mM L-glutamine and supplemented with either 10%non-heat-inactivated newborn calf serum (NBCS, Biochrom Ag) or inKaighn's Modification of Ham's F-12 Medium (ATCC 30-2004) containing 15%inactivated fetal bovine serum (FBS, Gibco Invitrogen), respectively.BALB/c 3T3 and NR8383 were seeded in 96-well plates at densities of˜3000 cells/well and 12000 cells/well, respectively. The cells wereincubated at 37° C. in a humidified atmosphere of 5% CO2 for 24 h. Inparallel, profiles pipes impregnated with either P(MAA-MBAA)nanoparticles or chlorinated ones were incubated with the growth mediumused (w/o serum addition) for each cell line for 24 h as well. On thefollowing day, BALB/c 3T3 cells were decanted from the growth mediumused in the first day, and were then added with 50 μl of the medium thatwas incubated with the different profiles and 50 μl of a fresh medium toprovide the cells with serum. For NR8383 cells, the procedure waschanged a bit in light of their non-adherent properties, hence to the 50μl of cells that were seeded a day before, 50 μl of the medium incubatedwith the profiles were added. One or three assays were conducted todetermine the viability of NR8383 and BALB/c 3T3 cells, respectively.The assays were done as follows:

Water Soluble Tetrazolium Assay (WST-1 Assay):

This assay examines the activity of mitochondrial dehydrogenase enzymes,using WST-1 Cell Proliferation Reagent (Roche). Briefly, 10 μl of WST-1reagent were added into each well followed by incubation at 37° C. 5%CO2 for 3 h (BALB/c 3T3 cells) or 1 h (NR8383 cells). After theincubation, the plates were shaken for 1 min and the absorption of theFormazan produced was detected at 450 nm.

Neutral Red Uptake (NRU) Assay:

This assay examines the ability of cells to incorporate neutral red dyein endosomes/lysosomes and vacuoles using neutral red solution (NR,Sigma). 48 h after the cells were exposed to the treated medium, themedium was removed of the wells followed by a wash with D-PBS (LonzaWalkersvillle, USA). 200 μl of NR solution were added to all wells andthe plates were incubated at 37° C., 5% CO2 for 3 h. After incubation,the NR solution was removed and washing with D-PBS was done. Then, 100μl of NR desorption solution (40 parts water, 50 parts ethanol, 10 partsacetic acid, freshly prepared) were added to all the wells. The plateswere shaken for 30 min while they were protected from light, and thenreading the absorption at 540 nm was done

Adenosine Triphosphate (ATP) Assay:

24 h after the cells were exposed to the treated medium, 5 μl of 10% TCAwere added to all the wells. Then, the plates were frozen at 80° C. foranother 24 h. The levels of ATP were evaluated via ATP determination kit(Molecular probes).

Results

The results, obtained with PE/P(MAA-MBAA)-Cl composite nanoparticlesprofiles incubated in Shafdan water, have led us to examine anypotential toxic effects that might be exerted by the chlorinatednanoparticles to the environment. The profiles were incubated withmedium for 24 h and then, the medium was used for the growth of mousefibroblasts BALB/c 3T3 and rat alveolar macrophages NR8383 cell lines.Three cytotoxicity assays were conducted with BALB/c 3T3 cells for WST-1(FIG. 47A), NRU (FIG. 47B), and ATP (FIG. 47C) measurements. For NR8383cells, only WST-1 assay was applied in light of their non-adherentcharacteristics. All assays performed with BALB/c 3T3 cells have shownthat profiles coated with either P(MAA-MBAA) nanoparticles or thechlorinated ones do not release any reagents that might impart toxiceffects to the cells (FIGS. 47 A-C). However, it seems like theviability of NR8383 cells was compromised a bit by chlorinated profiles,i.e. reduction of 28% in the viability in comparison to untreated cellsor to cells treated with medium that was incubated with profilecontaining P(MAA-MBAA) nanoparticles.

Although the invention has been described in conjunction with specificembodiments thereof, it is evident that many alternatives, modificationsand variations will be apparent to those skilled in the art.Accordingly, it is intended to embrace all such alternatives,modifications and variations that fall within the spirit and broad scopeof the appended claims.

All publications, patents and patent applications mentioned in thisspecification are herein incorporated in their entirety by referenceinto the specification, to the same extent as if each individualpublication, patent or patent application was specifically andindividually indicated to be incorporated herein by reference. Inaddition, citation or identification of any reference in thisapplication shall not be construed as an admission that such referenceis available as prior art to the present invention. To the extent thatsection headings are used, they should not be construed as necessarilylimiting.

What is claimed is:
 1. An article comprising a composition-of-matter ofcomprising a plurality of crosslinked polymeric backbones, wherein atleast 80% of said plurality of crosslinked polymeric backbones are in aform of non-aggregated particles characterized by a hydrodynamicdiameter of less than 500 nm, said crosslinked polymeric backbones beingrepresented by the general Formula I:([A₁]_(x)[A₂]_(y))B_(n) wherein: (a) A₁ is a monomeric unit derived froma secondary diamide compound, said secondary diamide compound beingrepresented by the general formula II:

such that R₁ and R₃ are hydrogen or a methyl group; and R₂ is C₁-C₄alkyl group; (b) A₂ is a monomeric unit being a primary amide selectedfrom the group consisting of: acrylamide, alkylacrylamide, and anyderivative thereof; (c) each of said plurality of polymeric backbones iscrosslinked by at least one A₁; (d) B, in each instance, is a halogenatom independently selected from the group consisting of Cl, Br, and I;(e) x and y are integers, independently, representing the total numbersof A₁ and A₂, respectively, in said plurality of crosslinked polymericbackbones, said x and said y having a value of at least 5: (f) nrepresents the total numbers of said B; (g) a weight ratio of A₁/A₂within said plurality of crosslinked polymeric backbones is at most 6/4;and wherein said composition is incorporated within, or coated on asurface of said article.
 2. The article of claim 1, being selected fromthe group consisting of a medical device, organic waste processingdevice, fluidic device, water system device, tubing, an agriculturaldevice, a package, a sealing article, a fuel container and aconstruction element.
 3. The article of claim 1, wherein said halogenatom, in one or more instances, is bound to the nitrogen belonging tosaid A₁ and/or to said A₂.
 4. A method of manufacturing thecomposition-of-matter of claim 1, comprising: providing a polymericmaterial comprising a plurality of crosslinked polymeric backbonescomprising a plurality of said monomeric units A₁ and A₂, characterizedby an average hydrodynamic diameter of less than 500 nm with; and atleast partially halogenating said polymeric material by an addition of ahalogen source, thereby obtaining a halogenated polymeric materialcomprising said halogen atom, in one or more instances, bound to anitrogen atom belonging to said A₁ and/or to said A₂.
 5. The method ofclaim 4, wherein said at least one water soluble initiator is selectedfrom the group consisting of: AIBNCO₂H, H₂O₂, potassium persulfate(PPS), and azobisisobutylonitrile (AIBN).
 6. The method of claim 4,wherein said surfactant-free aqueous phase further comprises one or morereducing agent selected from the group consisting of: a sulfite, abisulfate, thiosulfate, formamidinesulfinic acid, and ascorbic acid. 7.The method of claim 4, wherein said halogen source comprises a salt of amaterial selected from the group consisting of: di-X-isocyanurate,N—X-succinimide, or hypo-halite, wherein said halite and X each areeach, independently, selected from the group consisting of: Cl, I, orBr.
 8. The article of claim 1, wherein said n has a value such thatn/(x+y) multiplied by 100 is at least 0.1, or is
 0. 9. The article ofclaim 1, wherein any of nitrogen atoms belonging to said A₁ and/or tosaid A₂ is capable of forming a halamine bond with a halogen source. 10.The article of claim 9, wherein said halogen source comprises a salt ofa material selected from the group consisting of: di-X-isocyanurate,N—X-succinimide, or hypo-halite, wherein said halite and X each areeach, independently, selected from the group consisting of: Cl, I, orBr.
 11. The article of claim 1, wherein a weight ratio of A₁/A₂ withinsaid crosslinked polymeric backbone ranges from 1/8 to 6/4, and whereinsaid polymeric backbone is characterized by a size distribution of thatvaries within a range of less than 20%.
 12. The method of claim 4,wherein said polymeric material is prepared by co-polymerizing aplurality of said monomeric units, A₁ and A₂, said co-polymerizingcomprising dispersing said monomers in a weight ratio of A₁/A₂ thatranges from about 1/9 to about 6/4 in a surfactant-free aqueous phasecomprising at least one water soluble initiator.